[go: up one dir, main page]

US11342630B2 - Catholytes for solid state rechargeable batteries, battery architectures suitable for use with these catholytes, and methods of making and using the same - Google Patents

Catholytes for solid state rechargeable batteries, battery architectures suitable for use with these catholytes, and methods of making and using the same Download PDF

Info

Publication number
US11342630B2
US11342630B2 US16/326,852 US201716326852A US11342630B2 US 11342630 B2 US11342630 B2 US 11342630B2 US 201716326852 A US201716326852 A US 201716326852A US 11342630 B2 US11342630 B2 US 11342630B2
Authority
US
United States
Prior art keywords
examples
solvent
carbonate
catholyte
lithium
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active, expires
Application number
US16/326,852
Other versions
US20190198838A1 (en
Inventor
Greg Roberts
Zhebo Chen
Will Hudson
Rainer Fasching
Tiffany HO
Timothy P. Holme
Mohit Singh
Aram Yang
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Quantumscape Battery Inc
Original Assignee
Quantumscape Battery Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Quantumscape Battery Inc filed Critical Quantumscape Battery Inc
Priority to US16/326,852 priority Critical patent/US11342630B2/en
Assigned to QUANTUMSCAPE CORPORATION reassignment QUANTUMSCAPE CORPORATION ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: FASCHING, RAINER, ROBERTS, GREG, SINGH, MOHIT, HO, Tiffany, HUDSON, WILL, YANG, ARAM, CHEN, Zhebo, HOLME, TIMOTHY P.
Publication of US20190198838A1 publication Critical patent/US20190198838A1/en
Assigned to QUANTUMSCAPE SUBSIDIARY, INC. reassignment QUANTUMSCAPE SUBSIDIARY, INC. CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). Assignors: QUANTUMSCAPE CORPORATION
Assigned to QUANTUMSCAPE BATTERY, INC. reassignment QUANTUMSCAPE BATTERY, INC. CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). Assignors: QUANTUMSCAPE SUBSIDIARY, INC.
Application granted granted Critical
Publication of US11342630B2 publication Critical patent/US11342630B2/en
Active legal-status Critical Current
Adjusted expiration legal-status Critical

Links

Images

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/46Separators, membranes or diaphragms characterised by their combination with electrodes
    • H01M50/461Separators, membranes or diaphragms characterised by their combination with electrodes with adhesive layers between electrodes and separators
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/056Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/056Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
    • H01M10/0561Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of inorganic materials only
    • H01M10/0562Solid materials
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/056Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
    • H01M10/0564Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
    • H01M10/0566Liquid materials
    • H01M10/0567Liquid materials characterised by the additives
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/058Construction or manufacture
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/134Electrodes based on metals, Si or alloys
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/38Selection of substances as active materials, active masses, active liquids of elements or alloys
    • H01M4/381Alkaline or alkaline earth metals elements
    • H01M4/382Lithium
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/46Separators, membranes or diaphragms characterised by their combination with electrodes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0017Non-aqueous electrolytes
    • H01M2300/0025Organic electrolyte
    • H01M2300/0028Organic electrolyte characterised by the solvent
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0017Non-aqueous electrolytes
    • H01M2300/0065Solid electrolytes
    • H01M2300/0068Solid electrolytes inorganic
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0017Non-aqueous electrolytes
    • H01M2300/0065Solid electrolytes
    • H01M2300/0068Solid electrolytes inorganic
    • H01M2300/0071Oxides
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0085Immobilising or gelification of electrolyte
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0088Composites
    • H01M2300/0094Composites in the form of layered products, e.g. coatings
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

Definitions

  • the present disclosure sets forth high voltage-stable electrolytes, such as dinitrile solvents and mixtures of dinitrile solvents and nitrile solvents, and organic sulfur-including solvents which include lithium salts, electrochemical cells and devices which include these electrolytes, and methods of making and using the same.
  • an electrochemical cell which includes: a lithium metal negative electrode;
  • the positive electrode includes an active material and a catholyte
  • the catholyte includes a catholyte solvent and a lithium salt, wherein the catholyte solvent comprises a nitrile solvent, a dinitrile solvent, an organic sulfur-including solvent, or a combination thereof.
  • a catholyte including a nitrile solvent and a lithium salt
  • a catholyte comprising an organic sulfur-including solvent, optionally a co-solvent, and a lithium salt
  • set forth herein is a method of using an electrochemical cell set forth herein, comprising charging the electrochemical cell to a voltage greater than 4.3V.
  • set forth herein is a method of storing an electrochemical cell, including providing an electrochemical cell set forth herein, wherein the electrochemical cell has greater than 20% state-of-charge (SOC); and storing the battery for at least one day.
  • SOC state-of-charge
  • a method for making a catholyte set forth herein which includes a nitrile solvent and a lithium salt wherein the method includes providing a nitrile solvent, providing a lithium salt, mixing the nitrile solvent and the lithium salt to form a mixture, and optionally heating the mixture.
  • a method for making a catholyte set forth herein which includes an organic sulfur-including solvent and a lithium salt wherein the method includes providing an organic sulfur-including solvent, providing a lithium salt, mixing the organic sulfur-including solvent and the lithium salt to form a mixture, and optionally heating the mixture.
  • FIG. 1 shows a schematic of an example of an electrochemical cell having a catholyte in the positive electrode space which includes a dinitrile solvent.
  • FIG. 2 shows a plot of the median charge ASR-DC ( ⁇ -cm 2 ) for two electrochemical cells, after storage at 4.6 V, and wherein one electrochemical cell includes a catholyte including succinonitrile (SCN) at 12 mol % LiBF 4 and wherein the other electrochemical cell includes a catholyte including EC:EMC+1 M LiPF 6 +2 wt % monofluoroethylene carbonate (FEC).
  • circles refer to succinonitrile+12 mol % LiBF 4
  • triangles refer to EC:EMC+1 M LiPF 6 +2 wt % FEC.
  • Elyte in FIG. 2 refers to electrolyte.
  • EC refers to ethyl carbonate solvent.
  • EMC refers to ethyl methyl carbonate solvent.
  • FIG. 3 shows a plot of the median discharge ASR-DC ( ⁇ -cm 2 ) for two electrochemical cells, after storage at 4.6 V, and wherein one electrochemical cell includes a catholyte including succinonitrile (SCN) at 12 mol % LiBF 4 and wherein the other electrochemical cell includes a catholyte including EC:EMC+1 M LiPF 6 +2 wt % monofluoroethylene carbonate (FEC).
  • SCN succinonitrile
  • FEC monofluoroethylene carbonate
  • FIG. 4 shows a plot of active mass-specific discharge capacity (mAh/g) as a function of cycle index for devices made according to Example 2 with two different catholytes.
  • FIG. 5 shows a plot of the median charge and discharge ASR dc ( ⁇ -cm 2 ) for two electrochemical cells, both stored at 4.6 V, and wherein one electrochemical cell includes a catholyte including succinonitrile at 12 mol % LiBF 4 and wherein the other electrochemical cell includes a catholyte including EC:EMC+1 M LiPF 6 +2 wt % FEC.
  • circles refer to succinonitrile+12 mol % LiBF 4
  • triangles refer to EC:EMC at 3.7 w/w+1 M LiPF 6 +2 wt % FEC.
  • FIG. 6 shows a plot of mass percent of Gel Polymer Soaked in Electrolyte for two electrochemical cells, wherein one electrochemical cell includes a catholyte including adiponitrile and 1M LiTFSi and wherein the other electrochemical cell includes a catholyte including EC:EMC+1 M LiPF 6 +2 wt % FEC.
  • solid line is adiponitrile+1 M LiTFSi
  • doted line is EC:EMC+1 M LiPF 6 +2 wt % FEC.
  • FIG. 7 shows a plot of charge ASR growth wherein the cell is prepared with sulfolane and ethylene carbonate (3:7 v/v)+2M LiPF 6 vs ethyl-methyl carbonate, ethylene carbonate (3:7 v/v)+1M LiPF 6 for 10 cycles, C/3 pulses, from 2.7-4.2 V at 45° C.
  • the cathode is NMC
  • the separator is solid-state separator material.
  • Solid line is EC:EMC 3:7 v/v+1 MLiPF 6 ; dotted line is EC:Sulfolane 3:7 v/v+2 M LiPF 6 .
  • FIG. 8 shows a plot of discharge and charge ASR versus cycle life for 500 cycles for a cell.
  • the term “about,” when qualifying a number refers to the number qualified and optionally the numbers included in a range about that qualified number that includes ⁇ 10% of the number. For example, about 15% w/w includes 15% w/w as well as 13.5% w/w, 14% w/w, 14.5% w/w, 15.5% w/w, 16% w/w, or 16.5% w/w. For example, “about 75° C.,” includes 75° C.
  • Li + ion-conducting separator refers to an electrolyte which conducts Li + ions, is substantially insulating to electrons (e.g., the lithium ion conductivity is at least 10 3 times, and often 10 6 times, greater than the electron conductivity), and which acts as a physical barrier or spacer between the positive and negative electrodes in an electrochemical cell.
  • solid separator solid electrolyte
  • solid-state separator solid-state electrolyte
  • selected from the group consisting of refers to a single member from the group, more than one member from the group, or a combination of members from the group.
  • a member selected from the group consisting of A, B, and C includes, for example, A only, B only, or C only, as well as A and B, A and C, B and C, as well as A, B, and C.
  • electrochemical cell refers to, for example, a “battery cell” and includes a positive electrode, a negative electrode, and an electrolyte therebetween which conducts ions (e.g., Li + ) but electrically insulates the positive and negative electrodes.
  • a battery may include multiple positive electrodes and/or multiple negative electrodes enclosed in one container.
  • electrochemical stack refers to one or more units which each include at least a negative electrode (e.g., Li, LiC 6 ), a positive electrode (e.g., Li-nickel-manganese-oxide or FeF 3 , optionally combined with a solid-state electrolyte or a gel electrolyte), and a solid electrolyte (e.g., an oxide electrolyte set forth herein, a lithium-stuffed garnet film, or a lithium-stuffed garnet pellet) between and in contact with the positive and negative electrodes.
  • a compliant e.g., gel electrolyte
  • An electrochemical stack may include one of these aforementioned units.
  • An electrochemical stack may include several of these aforementioned units arranged in electrical communication (e.g., serial or parallel electrical connection).
  • the electrochemical stack includes several units, the units are layered or laminated together in a column.
  • the electrochemical stack includes several units, the units are layered or laminated together in an array.
  • the stacks are arranged such that one negative electrode is shared with two or more positive electrodes.
  • the electrochemical stack includes several units, the stacks are arranged such that one positive electrode is shared with two or more negative electrodes.
  • an electrochemical stack includes one positive electrode, one solid electrolyte, and one negative electrode, and optionally includes a gel electrolyte layer between the positive electrode and the solid electrolyte.
  • the gel electrolyte layer is also included in the positive electrode.
  • the gel electrolyte includes any electrolyte set forth herein, including a nitrile, dinitrile, organic sulfur-including solvent, or combination thereof set forth herein.
  • electrolytes refers to a material that allows ions, e.g., Li + , to migrate or conduct therethrough but which does not allow electrons to conduct therethrough. Electrolytes are useful for electrically isolating the cathode and anodes of a secondary battery while allowing ions, e.g., Li + , to transmit through the electrolyte. Solid electrolytes, in particular, rely on ion hopping through rigid structures. Solid electrolytes may be also referred to as fast ion conductors or super-ionic conductors.
  • Solid electrolytes may be also used for electrically insulating the positive and negative electrodes of a cell while allowing for the conduction of ions, e.g., Li + , through the electrolyte.
  • a solid electrolyte layer may be also referred to as a solid electrolyte separator or solid-state electrolyte separator.
  • gel electrolyte refers to a suitable Li + ion conducting gel or liquid-based electrolyte, for example, those set forth in U.S. Pat. No. 5,296,318, entitled RECHARGEABLE LITHIUM INTERCALATION BATTERY WITH HYBRID POLYMERIC ELECTROLYTE.
  • a gel electrolyte has a lithium ion conductivity of greater than 10 ⁇ 5 S/cm at room temperature, a lithium transference number between 0.05-0.95, and a storage modulus greater than the loss modulus at some temperature.
  • a gel electrolyte may comprise a polymer matrix, a solvent that gels the polymer, and a lithium containing salt that is at least partly dissociated into Li + ions and anions.
  • a gel electrolyte may comprise a porous polymer matrix, a solvent that fills the pores, and a lithium containing salt that is at least partly dissociated into Li + ions and anions where the pores have one length scale less than 10 ⁇ m.
  • the term “laminating” refers to the process of sequentially depositing a layer of one precursor specie, e.g., a lithium precursor specie, onto a deposition substrate and then subsequently depositing an additional layer onto an already deposited layer using a second precursor specie, e.g., a transition metal precursor specie. This laminating process can be repeated to build up several layers of deposited vapor phases.
  • the term “laminating” also refers to the process whereby a layer comprising an electrode, e.g., positive electrode or cathode active material comprising layer, is contacted to a layer comprising another material, e.g., garnet electrolyte.
  • laminating also refers to the process whereby at least two layers comprising a solid electrolyte material are contacted together.
  • the laminating process may include a reaction or use of a binder which adheres of physically maintains the contact between the layers which are laminated.
  • the process of laminating one layer to another layer results in one layer being laminated to the other layer.
  • direct contacts refers to the juxtaposition of two materials such that the two materials contact each other sufficiently to conduct either an ion or electron current.
  • direct contact refers to two materials in contact with each other and which do not have any materials positioned between the two materials which are in direct contact.
  • cathode and “anode” refer to the electrodes of a battery.
  • the cathode and anode are often referred to in the relevant field as the positive electrode and negative electrode, respectively.
  • Li ions leave the cathode and move through an electrolyte, to the anode.
  • electrons leave the cathode and move through an external circuit to the anode.
  • Li ions migrate towards the cathode through an electrolyte and from the anode.
  • electrons leave the anode and move through an external circuit to the cathode.
  • positive electrode refers to the electrode in a secondary battery towards which positive ions, e.g., Li + , conduct, flow or move during discharge of the battery.
  • negative electrode refers to the electrode in a secondary battery from where positive ions, e.g., Li + , flow or move during discharge of the battery.
  • the electrode having the conversion chemistry, intercalation chemistry, or combination conversion/intercalation chemistry material is referred to as the positive electrode.
  • cathode is used in place of positive electrode, and anode is used in place of negative electrode.
  • Li ions move from the positive electrode (e.g., NiF x , NMC, NCA) towards the negative electrode (e.g., Li-metal).
  • the positive electrode e.g., NiF x , NMC, NCA
  • the negative electrode e.g., Li-metal
  • Li ions move towards the positive electrode and from the negative electrode.
  • Catholyte refers to a Li ion conductor that is intimately mixed with, or that surrounds and contacts, or that contacts the positive electrode active materials and provides an ionic pathway for Li + to and from the active materials.
  • Catholytes suitable with the embodiments described herein include, but are not limited to, catholytes having the acronyms name LPS, LXPS, LXPSO, where X is Si, Ge, Sn, As, Al, LATS, or also Li-stuffed garnets, or combinations thereof, and the like.
  • Catholytes may also be liquid, gel, semi-liquid, semi-solid, polymer, and/or solid polymer ion conductors known in the art.
  • the catholyte includes a gel set forth herein.
  • the gel electrolyte includes any electrolyte set forth herein, including a nitrile, dinitrile, organic sulfur-including solvent, or combination thereof set forth herein.
  • the electrolytes herein may include, or be layered with, or be laminated to, or contact a sulfide electrolyte.
  • sulfide electrolyte includes, but is not limited to, electrolytes referred to herein as LSS, LTS, LXPS, or LXPSO, where X is Si, Ge, Sn, As, Al, LATS.
  • LSS, LTS, LXPS, or LXPSO S refers to the element S, Si, or combinations thereof
  • T refers to the element Sn.
  • “Sulfide electrolyte” may also include Li a P b S c X d , Li a B b S c X d , Li a Sn b S c X d or Li a Si b S c X d where X ⁇ F, Cl, Br, I, and 10% ⁇ a ⁇ 50%, 10% ⁇ b ⁇ 44%, 24% ⁇ c ⁇ 70%, 0 ⁇ d ⁇ 18% and may further include oxygen in small amounts. For example, oxygen may be present as a dopant or in an amount less than 10 percent by weight. For example, oxygen may be present as a dopant or in an amount less than 5 percent by weight.
  • sulfide based electrolytes refers to electrolytes that include inorganic materials containing S which conduct ions (e.g., Li + ) and which are suitable for electrically insulating the positive and negative electrodes of an electrochemical cell (e.g., secondary battery).
  • sulfide electrolyte includes, but are not limited to, LSS, LTS, LXPS, LXPSO, where X is Si, Ge, Sn, As, Al, LATS, also Li-stuffed garnets, or combinations thereof, and the like, S is S, Si, or combinations thereof, T is Sn.
  • SLOPS includes, unless otherwise specified, a 60:40 molar ratio of Li 2 S:SiS 2 with 0.1-10 mol. % Li 3 PO 4 .
  • SLOPS includes Li 10 Si 4 S 13 (50:50 Li 2 S:SiS 2 ) with 0.1-10 mol. % Li 3 PO 4 .
  • SLOPS includes Li 26 Si 7 S 27 (65:35 Li 2 S:SiS 2 ) with 0.1-10 mol. % Li 3 PO 4 .
  • SLOPS includes Li 4 SiS 4 (67:33 Li 2 S:SiS 2 ) with 0.1-5 mol. % Li 3 PO 4 .
  • “SLOPS” includes Li 14 Si 3 S 13 (70:30 Li 2 S:SiS 2 ) with 0.1-5 mol. % Li 3 PO 4 .
  • “SLOPS” is characterized by the formula (1 ⁇ x)(60:40 Li 2 S:SiS 2 )*(x)(Li 3 PO 4 ), wherein x is from 0.01 to 0.99.
  • “LBS-POX” refers to an electrolyte composition of Li 2 S:B 2 S 3 :Li 3 PO 4 :LiX where X is a halogen (X ⁇ F, Cl, Br, I).
  • the composition can include Li 3 BS 3 or Li 5 B 7 S 13 doped with 0-30% lithium halide such as LiI and/or 0-10% Li 3 PO 4 .
  • LBS refers to an electrolyte material characterized by the formula Li a B b S c and may include oxygen and/or a lithium halide (LiF, LiCl, LiBr, LiI) at 0-40 mol %.
  • LPSO refers to an electrolyte material characterized by the formula Li x P y S z O w where 0.33 ⁇ x ⁇ 0.67, 0.07 ⁇ y ⁇ 0.2, 0.4 ⁇ z ⁇ 0.55, 0 ⁇ w ⁇ 0.15.
  • LPS LPS, as defined above, that includes an oxygen content of from 0.01 to 10 atomic %.
  • the oxygen content is 1 atomic %.
  • the oxygen content is 2 atomic %.
  • the oxygen content is 3 atomic %.
  • the oxygen content is 4 atomic %.
  • the oxygen content is 5 atomic %.
  • the oxygen content is 6 atomic %.
  • the oxygen content is 7 atomic %.
  • the oxygen content is 8 atomic %.
  • the oxygen content is 9 atomic %.
  • the oxygen content is 10 atomic %.
  • LIRAP refers to a lithium rich antiperovskite and is used synonymously with “LOC” or “Li 3 OCl”.
  • LSS refers to lithium silicon sulfide which can be described as Li 2 S—SiS 2 , Li—SiS 2 , Li—S—Si, and/or a catholyte consisting essentially of Li, S, and Si.
  • LSS refers to an electrolyte material characterized by the formula Li x Si y S z where 0.33 ⁇ x ⁇ 0.5, 0.1 ⁇ y ⁇ 0.2, 0.4 ⁇ z ⁇ 0.55, and it may include up to 10 atomic % oxygen.
  • LSS also refers to an electrolyte material comprising Li, Si, and S. In some examples, LSS is a mixture of Li 2 S and SiS 2 .
  • the ratio of Li 2 S:SiS 2 is 90:10, 85:15, 80:20, 75:25, 70:30, 2:1, 65:35, 60:40, 55:45, or 50:50 molar ratio.
  • LSS may be doped with compounds such as Li x PO y , Li x BO y , Li 4 SiO 4 , Li 3 MO 4 , Li 3 MO 3 , PS x , and/or lithium halides such as, but not limited to, LiI, LiCl, LiF, or LiBr, wherein 0 ⁇ x ⁇ 5 and 0 ⁇ y ⁇ 5.
  • LTS refers to a lithium tin sulfide compound which can be described as Li 2 S—SnS 2 , Li 2 S—SnS, Li—S—Sn, and/or a catholyte consisting essentially of Li, S, and Sn.
  • the composition may be Li x Sn y S z where 0.25 ⁇ x ⁇ 0.65, 0.05 ⁇ y ⁇ 0.2, and 0.25 ⁇ z ⁇ 0.65.
  • LTS is a mixture of Li 2 S and SnS 2 in the ratio of 80:20, 75:25, 70:30, 2:1, or 1:1 molar ratio.
  • LTS may include up to 10 atomic % oxygen.
  • LTS may be doped with Bi, Sb, As, P, B, Al, Ge, Ga, and/or In.
  • LATS refers to LTS, as used above, and further comprising Arsenic (As).
  • LXPS refers to a material characterized by the formula Li a MP b S c , where M is Si, Ge, Sn, and/or Al, and where 2 ⁇ a ⁇ 8, 0.5 ⁇ b ⁇ 2.5, 4 ⁇ c ⁇ 12.
  • LSPS refers to an electrolyte material characterized by the formula L a SiP b S c , where 2 ⁇ a ⁇ 8, 0.5 ⁇ b ⁇ 2.5, 4 ⁇ c ⁇ 12.
  • LSPS refers to an electrolyte material characterized by the formula L a SiP b S c , wherein, where 2 ⁇ a ⁇ 8, 0.5 ⁇ b ⁇ 2.5, 4 ⁇ c ⁇ 12, d ⁇ 3.
  • Exemplary LXPS materials are found, for example, in International Patent Application No.
  • LSTPSO refers to LSTPS that is doped with, or has, O present. In some examples, “LSTPSO” is a LSTPS material with an oxygen content between 0.01 and 10 atomic %. “LSPS” refers to an electrolyte material having Li, Si, P, and S chemical constituents. As used herein “LSTPS” refers to an electrolyte material having Li, Si, P, Sn, and S chemical constituents. As used herein, “LSPSO” refers to LSPS that is doped with, or has, O present. In some examples, “LSPSO” is a LSPS material with an oxygen content between 0.01 and 10 atomic %.
  • LATP refers to an electrolyte material having Li, As, Sn, and P chemical constituents.
  • LAGP refers to an electrolyte material having Li, As, Ge, and P chemical constituents.
  • LXPSO refers to a catholyte material characterized by the formula Li a MP b S c O d , where M is Si, Ge, Sn, and/or Al, and where 2 ⁇ a ⁇ 8, 0.5 ⁇ b ⁇ 2.5, 4 ⁇ c ⁇ 12, d ⁇ 3.
  • LXPSO refers to LXPS, as defined above, and having oxygen doping at from 0.1 to about 10 atomic %.
  • LPSO refers to LPS, as defined above, and having oxygen doping at from 0.1 to about 10 atomic %.
  • LPS refers to an electrolyte having Li, P, and S chemical constituents.
  • LPSO refers to LPS that is doped with or has O present.
  • LPSO is a LPS material with an oxygen content between 0.01 and 10 atomic %.
  • LPS refers to an electrolyte material that can be characterized by the formula Li x P y S z where 0.33 ⁇ x ⁇ 0.67, 0.07 ⁇ y ⁇ 0.2 and 0.4 ⁇ z ⁇ 0.55.
  • LPS also refers to an electrolyte characterized by a product formed from a mixture of Li 2 S:P 2 S 5 wherein the molar ratio is 10:1, 9:1, 8:1, 7:1, 6:1 5:1, 4:1, 3:1, 7:3, 2:1, or 1:1.
  • LPS also refers to an electrolyte characterized by a product formed from a mixture of Li 2 S:P 2 S 5 wherein the reactant or precursor amount of Li 2 S is 95 atomic % and P 2 S 5 is 5 atomic %.
  • LPS also refers to an electrolyte characterized by a product formed from a mixture of Li 2 S:P 2 S 5 wherein the reactant or precursor amount of Li 2 S is 90 atomic % and P 2 S 5 is 10 atomic %.
  • LPS also refers to an electrolyte characterized by a product formed from a mixture of Li 2 S:P 2 S 5 wherein the reactant or precursor amount of Li 2 S is 85 atomic % and P 2 S 5 is 15 atomic %.
  • LPS also refers to an electrolyte characterized by a product formed from a mixture of Li 2 S:P 2 S 5 wherein the reactant or precursor amount of Li 2 S is 80 atomic % and P 2 S 5 is 20 atomic %.
  • LPS also refers to an electrolyte characterized by a product formed from a mixture of Li 2 S:P 2 S 5 wherein the reactant or precursor amount of Li 2 S is 75 atomic % and P 2 S 5 is 25 atomic %.
  • LPS also refers to an electrolyte characterized by a product formed from a mixture of Li 2 S:P 2 S 5 wherein the reactant or precursor amount of Li 2 S is 70 atomic % and P 2 S 5 is 30 atomic %.
  • LPS also refers to an electrolyte characterized by a product formed from a mixture of Li 2 S:P 2 S 5 wherein the reactant or precursor amount of Li 2 S is 65 atomic % and P 2 S 5 is 35 atomic %.
  • LPS also refers to an electrolyte characterized by a product formed from a mixture of Li 2 S:P 2 S 5 wherein the reactant or precursor amount of Li 2 S is 60 atomic % and P 2 S 5 is 40 atomic %.
  • rational number refers to any number which can be expressed as the quotient or fraction (e.g., p/q) of two integers (e.g., p and q), with the denominator (e.g., q) not equal to zero.
  • quotient or fraction e.g., p/q
  • denominator e.g., q
  • Example rational numbers include, but are not limited to, 1, 1.1, 1.52, 2, 2.5, 3, 3.12, and 7.
  • lithium stuffed garnet refers to oxides that are characterized by a crystal structure related to a garnet crystal structure.
  • This application describes Li-stuffed garnet solid-state electrolytes used in solid-state lithium rechargeable batteries.
  • Li-stuffed garnets generally having a composition according to Li A La B M′ C M′′ D Zr E O F , Li A La B M′ C M′′ D Ta E O F , or Li A La B M′ C M′′ D Nb E O F , wherein 4 ⁇ A ⁇ 8.5, 1.5 ⁇ B ⁇ 4, 0 ⁇ C ⁇ 2, 0 ⁇ D ⁇ 2; 0 ⁇ E ⁇ 2.5, 10 ⁇ F ⁇ 13, and M′ and M′′ are each, independently in each instance selected from Ga, Al, Mo, W, Nb, Sb, Ca, Ba, Sr, Ce, Hf, Rb, and Ta, or Li a La b Zr c Al d Me′′ e O f , wherein 5 ⁇ a ⁇ 8.5; 2 ⁇ b ⁇ 4; 0 ⁇ c ⁇ 2.5; 0 ⁇ d ⁇ 2; 0 ⁇ e ⁇ 2, and 10 ⁇ f ⁇ 13 and Me′′ is a metal selected from Ga, Nb, Ta, V, W, Mo, and Sb and as otherwise described in U.S.
  • garnets used herein include, but are not limited to, Li x La 3 Zr 2 O F +yAl 2 O 3 , wherein x ranges from 5.5 to 9; and y ranges from 0.05 to 1.
  • subscripts x, y, and F are selected so that the garnet is charge neutral.
  • x is 7 and y is 1.0.
  • x is 5 and y is 1.0.
  • x is 6 and y is 1.0.
  • x is 8 and y is 1.0.
  • x is 9 and y is 1.0.
  • x is 7 and y is 0.35.
  • x is 5 and y is 0.35.
  • x is 6 and y is 0.35.
  • x is 8 and y is 0.35.
  • x is 9 and y is 0.35.
  • x is 7 and y is 0.35.
  • x is 5 and y is 0.35.
  • x is 6 and y is 0.35.
  • x is 8 and y is 0.35.
  • x is 9 and y is 0.35.
  • x is 7 and y is 0.7.
  • x is 5 and y is 0.7. In some examples, x is 6 and y is 0.7. In some examples, x is 8 and y is 0.7. In some examples, x is 9 and y is 0.7. In some examples x is 7 and y is 0.75. In some examples, x is 5 and y is 0.75. In some examples, x is 6 and y is 0.75. In some examples, x is 8 and y is 0.75. In some examples, x is 9 and y is 0.75. In some examples x is 7 and y is 0.8. In some examples, x is 5 and y is 0.8. In some examples, x is 6 and y is 0.8.
  • x is 8 and y is 0.8. In some examples, x is 9 and y is 0.8. In some examples x is 7 and y is 0.5. In some examples, x is 5 and y is 0.5. In some examples, x is 6 and y is 0.5. In some examples, x is 8 and y is 0.5. In some examples, x is 9 and y is 0.5. In some examples x is 7 and y is 0.4. In some examples, x is 5 and y is 0.4. In some examples, x is 6 and y is 0.4. In some examples, x is 8 and y is 0.4. In some examples, x is 9 and y is 0.4. In some examples x is 7 and y is 0.3.
  • x is 5 and y is 0.3. In some examples, x is 6 and y is 0.3. In some examples, x is 8 and y is 0.3. In some examples, x is 9 and y is 0.3. In some examples x is 7 and y is 0.22. In some examples, x is 5 and y is 0.22. In some examples, x is 6 and y is 0.22. In some examples, x is 8 and y is 0.22. In some examples, x is 9 and y is 0.22. Also, garnets as used herein include, but are not limited to, Li x La 3 Zr 2 O 12 +yAl 2 O 3 .
  • the Li-stuffed garnet herein has a composition of Li 7 Li 3 Zr 2 O 12 . In another embodiment, the Li-stuffed garnet herein has a composition of Li 7 Li 3 Zr 2 O 12 .Al 2 O 3 . In yet another embodiment, the Li-stuffed garnet herein has a composition of Li 7 Li 3 Zr 2 O 12 0.22Al 2 O 3 . In yet another embodiment, the Li-stuffed garnet herein has a composition of Li 7 Li 3 Zr 2 O 12 .0.35Al 2 O 3 . In certain other embodiments, the Li-stuffed garnet herein has a composition of Li 7 Li 3 Zr 2 O 12 .0.5Al 2 O 3 . In another embodiment, the Li-stuffed garnet herein has a composition of Li 7 Li 3 Zr 2 O 12 .0.75Al 2 O 3 .
  • garnet does not include YAG-garnets (i.e., yttrium aluminum garnets, or, e.g., Y 3 Al 5 O 12 ).
  • garnet does not include silicate-based garnets such as pyrope, almandine, spessartine, grossular, hessonite, or cinnamon-stone, tsavorite, uvarovite and andradite and the solid solutions pyrope-almandine-spessarite and uvarovite-grossular-andradite.
  • Garnets herein do not include nesosilicates having the general formula X 3 Y 2 (SiO 4 ) 3 wherein X is Ca, Mg, Fe, and, or, Mn; and Y is Al, Fe, and, or, Cr.
  • inorganic solid-state electrolyte is used interchangeably with the phrase “solid separator” refers to a material which does not include carbon and which conducts atomic ions (e.g., Li + ) but does not conduct electrons.
  • An inorganic solid-state electrolyte is a solid material suitable for electrically isolating the positive and negative electrodes of a lithium secondary battery while also providing a conduction pathway for lithium ions.
  • Example inorganic solid-state electrolytes include oxide electrolytes and sulfide electrolytes, which are further defined below. Non-limiting example sulfide electrolytes are found, for example, in U.S. Pat. No. 9,172,114, which issued Oct.
  • Non-limiting example oxide electrolytes are found, for example, in US Patent Application Publication No. 2015-0200420 A1, which published Jul. 16, 2015.
  • the inorganic solid-state electrolyte also includes a polymer.
  • examples of the materials in International Patent Application PCT Patent Application Nos. PCT/US2014/059575 and PCT/US2014/059578, GARNET MATERIALS FOR LI SECONDARY BATTERIES AND METHODS OF MAKING AND USING GARNET MATERIALS, filed Oct. 7, 2014, which is incorporated by reference herein in its entirety, are suitable for use as the inorganic solid-state electrolytes described herein, also as the oxide based electrolytes, described herein, and also as the garnet electrolytes, described herein.
  • the phrase “casting a film” refers to the process of delivering or transferring a liquid or a slurry into a mold, or onto a substrate, such that the liquid or the slurry forms, or is formed into, a film. Casting may be done via doctor blade, Meyer rod, comma coater, gravure coater, microgravure, reverse comma coater, slot dye, slip and/or tape casting, and other methods known to those skilled in the art.
  • slot casting refers to a deposition process whereby a substrate is coated, or deposited, with a solution, liquid, slurry, or the like by flowing the solution, liquid, slurry, or the like, through a slot or mold of fixed dimensions that is placed adjacent to, in contact with, or onto the substrate onto which the deposition or coating occurs.
  • slot casting includes a slot opening of about 1 ⁇ m to 100 ⁇ m in slot opening width.
  • dip casting or “dip coating” refers to a deposition process whereby substrate is coated, or deposited, with a solution, liquid, slurry, or the like, by moving the substrate into and out of the solution, liquid, slurry, or the like, often in a vertical fashion.
  • making refers to the process or method of forming or causing to form the object that is made.
  • making an energy storage electrode includes the process, process steps, or method of causing the electrode of an energy storage device to be formed.
  • the end result of the steps constituting the making of the energy storage electrode is the production of a material that is functional as an electrode.
  • providing refers to the provision of, generation or, presentation of, or delivery of that which is provided.
  • garnet-type electrolyte refers to an electrolyte that includes a garnet or lithium stuffed garnet material described herein as the ionic conductor.
  • antiperovskite refers to an electrolyte characterized by the antiperovskite crystal structure.
  • Exemplary antiperovskites are found, for example, in U.S. patent application Ser. No. 13/777,602, filed Feb. 26, 2013.
  • Antiperovskites include but are not limited to Li 3 OBr or Li 3 OCl.
  • the phrase “subscripts and molar coefficients in the empirical formulas are based on the quantities of raw materials initially batched to make the described examples” means the subscripts, (e.g., 7, 3, 2, 12 in Li 7 La 3 Zr 2 O 12 and the coefficient 0.35 in 0.35Al 2 O 3 ) refer to the respective elemental ratios in the chemical precursors (e.g., LiOH, La 2 O 3 , ZrO 2 , Al 2 O 3 ) used to prepare a given material, (e.g., Li 7 La 3 Zr 2 O 12 .0.35Al 2 O 3 ).
  • the phrase “characterized by the formula” refers to a molar ratio of constituent atoms either as batched during the process for making that characterized material or as empirically determined.
  • solvent refers to a liquid that is suitable for dissolving or solvating a component or material described herein.
  • a solvent includes a liquid, e.g., propylene carbonate, which is suitable for dissolving a component, e.g., the salt, used in the electrolyte.
  • removing a solvent refers to the process whereby a solvent is extracted or separated from the components or materials set forth herein.
  • Removing a solvent includes, but is not limited to, evaporating a solvent.
  • Removing a solvent includes, but is not limited to, using a vacuum or a reduced pressure to drive off a solvent from a mixture, e.g., an unsintered thin film.
  • a thin film that includes a binder and a solvent is heated or also optionally placed in a vacuum or reduced atmosphere environment in order to evaporate the solvent to leave the binder, which was solvated, in the thin film after the solvent is removed.
  • Nitrile or “nitrile solvent” refers to a hydrocarbon substituted by a cyano group, or a solvent which includes a cyano (i.e., —C ⁇ N) substituent bonded to the solvent.
  • Nitrile solvents may include dinitrile solvents.
  • dinitrile or “dinitrile solvent” refers to a linear hydrocarbon chain where both ends of the chain are terminated with a cyano (i.e., —C ⁇ N) group.
  • Example dinitrile solvents are characterized by Formula (I):
  • R 1 , R 2 , R 3 , and R 4 are, independently in each instance, selected from —CN, —NO 2 , —CO 2 , —SO 4 , —H, —SO 3 , —SO 2 , —CH 2 —SO 3 , —CHF—SO 3 , —CF 2 —SO 3 , —F, —Cl, —Br, and —I; and wherein subscript m is an integer from 1 to 1000.
  • exemplary nitrile and dinitrile solvents include, but are not limited to, acetonitrile, succinonitrile, glutaronitrile, malononitrile, hexanedinitrile (adiponitrile), sebaconitrile, suberonitrile, pimelonitrile, dodecanedinitrile, phthalonitrile, cis/trans-1,2-dicyanocyclohexane, and combinations thereof.
  • organic sulfur-including solvent refers to a solvent selected from ethyl methyl sulfone, dimethyl sulfone, sulfolane, allyl methyl sulfone, butadiene sulfone, butyl sulfone, methyl methanesulfonate, and dimethyl sulfite.
  • the phrase “impermeable to the catholyte” refers to a material that allows a low flux of catholyte to permeate, for example less than 1 g/cm 2 /year, through the material, e.g., a solid separator, which is impermeable to the catholyte or its constituent components.
  • bonding layer refers to an ionically conductive layer between two other layers, e.g., between the cathode and the solid separator.
  • Exemplary bonding layers include the gel electrolytes, and related separator bonding agents, set forth in U.S. Provisional Patent Application No. 62/336,474, filed May 13, 2016, the entire contents of which are herein incorporated by reference in its entirety for all purposes.
  • HOMO or “Highest Occupied Molecular Orbital” refers to the energy of the electron occupying the highest occupied molecular orbital, as referenced to the vacuum energy.
  • LUMO refers to “Lowest Unoccupied Molecular Orbital.” HOMO and LUMO energy levels are calculated by DFT calculations referenced to the vacuum level. Unless otherwise specified, the DFT calculations use a B3LYP functional for exchange and correlation and a 6-311++g** basis set.
  • lithium transference refers to the proportion of current carried by lithium ions relative to the total current. Lithium transference is a number between 0 and 1, inclusive and may be measured by the Bruce-Vincent method.
  • the phrase “stability window” refers to the voltage range within which a material exhibits no reaction which materially or significantly degrades the material's function in an electrochemical cell. It may be measured in an electrochemical cell by measuring cell resistance and Coulombic efficiency during charge/discharge cycling. For voltages within the stability window (i.e. the working electrode vs reference electrode within the stability window), the increase of cell resistance is low. For example, this resistance increase may be less than 1% per 100 cycles.
  • LiBOB refers to lithium bis(oxalato)borate.
  • LiBETI refers to lithium bis(perfluoroethanesulfonyl)imide.
  • LIFSI lithium bis(fluorosulfonyl)imide
  • LiTFSI lithium bis-trifluoromethanesulfonimide
  • V vs. Li lithium metal
  • LiBHI refers to a combination of LiBH 4 and LiX, wherein X is Br, Cl, I, or a combination thereof.
  • LiBNHI refers to a combination of LiBH 4 , LiNH 2 , and LiX, wherein X is Br, Cl, I, or combinations thereof.
  • LiBHCl refers to a combination of LiBH 4 and LiCl.
  • LiBNHCl refers to a combination of LiBH 4 , LiNH 2 , and LiCl.
  • LiBHBr refers to a combination of LiBH 4 and LiBr.
  • LiBNHBr refers to a combination of LiBH 4 , LiNH 2 , and LiBr.
  • viscosity is measured using a Brookfield viscometer DV2T.
  • the term “monolith” refers to a shaped, fabricated article with a homogenous microstructure with no structural distinctions observed optically, which has a form factor top surface area between 10 cm 2 and 500 cm 2 .
  • vapor pressure refers to the equilibrium pressure of a gas above its liquid at the same temperature in a closed system. Measurement procedures often consist of purifying the test substance, isolating it in a container, evacuating any foreign gas, then measuring the equilibrium pressure of the gaseous phase of the substance in the container at different temperatures. Better accuracy is achieved when care is taken to ensure that the entire substance and its vapor are at the prescribed temperature. This is often done, as with the use of an isoteniscope, by submerging the containment area in a liquid bath.
  • lithium salt refers to a lithium-containing compound that is a solid at room temperature that at least partially dissociates when immersed in a solvent such as EMC.
  • Lithium salts may include but are not limited to LiPF 6 , LiBOB, LiTFSi, LiFSI, LiAsF 6 , LiClO 4 , LiI, LiBETI, LiBF 4 .
  • carbonate solvent refers to a class of solvents containing a carbonate group C( ⁇ O)(O—) 2 .
  • Carbonate solvents include but are not limited to ethylene carbonate, dimethyl carbonate, propylene carbonate, diethyl carbonate, ethyl methyl carbonate, dimethyl ethylene carbonate, isobutylene carbonate, nitroethyl carbonate, Monofluoroethylene carbonate, fluoromethyl ethylene carbonate, 1,2-butylene carbonate, methyl propyl carbonate, isopropyl methyl carbonate, etc.
  • a high voltage-stable catholyte refers to a catholyte which does not react at high voltage (4.2 V or higher versus Li metal) in a way that materially or significantly degrades the ionic conductivity of the catholyte when held at high voltage at room temperature for one week.
  • a material or significant degradation in ionic conductivity is a reduction in ionic conductivity by an order of magnitude or more.
  • the catholyte has an ionic conductivity of 10E-3 S/cm, and when charged to 4.2V or higher the catholyte has an ionic conductivity of 10E-4 S/cm, then the catholyte is not stable at 4.2V or higher since its ionic conductivity materially and significantly degraded at that voltage.”
  • the term “high voltage” means at least 4.2V versus lithium metal. High voltage may also refer to higher voltage, e.g., 4.3, 4.4, 4.5, 4.6, 4.7, 4.8. 4.9, 5.0 V or higher.
  • electrochemical performance refers to either ionic conductivity or area-specific resistance (ASR).
  • a material or significant degradation in ionic conductivity is a degradation by an order of magnitude or more.
  • a material or significant degradation in ASR is a degradation by a factor of 2 or more when held at room temperature for one week.
  • ASR is measured by electrochemical cycling using Arbin or Biologic unless otherwise specified to the contrary.
  • ionic conductivity is measured by electrical impedance spectroscopy methods known in the art.
  • battery architectures for batteries which include a solid-state separator which physically isolates the cathode from the anode.
  • These architectures allow, for the first time in a rechargeable lithium battery, the use of electrolytes in the cathode, i.e., catholytes, that have no stability requirement against lithium metal or graphite, e.g., high-voltage (greater than 4.3V) stable dinitrile electrolytes.
  • electrolytes have advantageous properties including safety, lifetime, cyclability, voltage stability, and rate performance.
  • set forth herein are devices that include a high voltage, nitrile, or dinitrile or organic sulfur-including cathode-electrolyte (i.e., catholyte) which is stable at high oxidation potentials within the cathode side of an electrochemical device having a solid-state separator.
  • catholyte organic sulfur-including cathode-electrolyte
  • the new battery architectures presented for the first time herein are not possible in a conventional Li-ion battery.
  • Conventional battery architectures use catholytes which penetrate the anode space and therefore must be stable and/or passivating at the anode voltage and also chemically compatible with the anode materials.
  • nitrile and high voltage-stable catholytes herein can be used practically in electrochemical devices as catholytes or electrolytes within the cathode space.
  • nitrile catholytes which are stable at high voltages with respect to lithium but which are not stable at low voltages with respect to lithium.
  • organic sulfur-including catholytes which are stable at high voltages with respect to lithium but which are not stable at low voltages (e.g. less than 1.5V or less than 1V) with respect to lithium, meaning that they significantly degrade in impedance or conductivity at room temperature for one week.
  • an electrochemical cell ( 100 ) includes a positive electrode 101 of 5-200 ⁇ m thickness.
  • This electrode 101 includes active materials 102 surrounded by a cathode-electrolyte 103 .
  • Active materials 102 may be present in 20-80 vol %, and the catholyte may be present in 5-60 vol %.
  • the electrode 101 is layered to a solid separator 104 (e.g., a lithium-stuffed garnet electrolyte monolith or thin film).
  • the solid separator 104 is layered to a lithium-metal negative electrode 105 .
  • the solid separator 104 may be 100 nm-100 ⁇ m thick, and the lithium metal negative electrode 105 may be 1 ⁇ m-50 ⁇ m thick.
  • the solid separator 104 is impermeable to the catholyte-electrolyte 103 .
  • the positive electrode is from 30 ⁇ m to 300 ⁇ m thick. In some examples, the positive electrode is from 40 ⁇ m to 200 ⁇ m thick. In some of these examples, the positive electrode is about 30 ⁇ m thick. In some of these examples, the positive electrode is about 40 ⁇ m thick. In some of these examples, the positive electrode is about 50 ⁇ m thick. In some of these examples, the positive electrode is about 60 ⁇ m thick. In some of these examples, the positive electrode is about 70 ⁇ m thick. In some of these examples, the positive electrode is about 80 ⁇ m thick. In some of these examples, the positive electrode is about 90 ⁇ m thick. In some of these examples, the positive electrode is about 100 ⁇ m thick.
  • the positive electrode is about 110 ⁇ m thick. In some of these examples, the positive electrode is about 120 ⁇ m thick. In some of these examples, the positive electrode is about 130 ⁇ m thick. In some of these examples, the positive electrode is about 140 ⁇ m thick. In some of these examples, the positive electrode is about 150 ⁇ m thick. In some of these examples, the positive electrode is about 160 ⁇ m thick. In some of these examples, the positive electrode is about 170 ⁇ m thick. In some of these examples, the positive electrode is about 180 ⁇ m thick. In some of these examples, the positive electrode is about 190 ⁇ m thick. In some of these examples, the positive electrode is about 200 ⁇ m thick. In some of these examples, the positive electrode is about 210 ⁇ m thick.
  • the positive electrode is about 220 ⁇ m thick. In some of these examples, the positive electrode is about 230 ⁇ m thick. In some of these examples, the positive electrode is about 240 ⁇ m thick. In some of these examples, the positive electrode is about 250 ⁇ m thick. In some of these examples, the positive electrode is about 260 ⁇ m thick. In some of these examples, the positive electrode is about 270 ⁇ m thick. In some of these examples, the positive electrode is about 280 ⁇ m thick. In some of these examples, the positive electrode is about 290 ⁇ m thick. In some of these examples, the positive electrode is about 300 ⁇ m thick.
  • the active material e.g., a nickel manganese cobalt oxide, i.e., NMC, a nickel cobalt aluminum oxide, i.e., NCA, a lithium cobalt oxide, i.e., LCO, a lithium-rich nickel manganese oxide, i.e., LNMO, FeF 3 , CoF 2 , CuF 2 , CoF 3 , and related or functionally equivalent active materials
  • a nickel manganese cobalt oxide i.e., NMC
  • a nickel cobalt aluminum oxide i.e., NCA
  • a lithium cobalt oxide i.e., LCO
  • a lithium-rich nickel manganese oxide i.e., LNMO
  • FeF 3 , CoF 2 , CuF 2 , CoF 3 and related or functionally equivalent active materials
  • the cathode electrolyte, or catholyte may be present in a volume fraction of 10-50%.
  • the catholyte is present in a volume fraction of 20-40 volume %.
  • the solid separator may be 0.5-100 ⁇ m thick. In some examples, the solid separator is 1-30 ⁇ m thick.
  • the negative electrode may be 3-80 ⁇ m thick. In some examples, the negative electrode is 20-50 ⁇ m thick in the charged state.
  • the carbon content in the positive electrode is less than 5% w/w. In any of the above examples, the binder content in the positive electrode is less than 5% w/w.
  • a high voltage-stable catholyte which includes a solvent and a lithium salt.
  • the solvent is a nitrile solvent.
  • the solvent is a dinitrile solvent.
  • the solvent is a combination of a nitrile and dinitrile solvent.
  • the solvent is a combination of a dinitrile and another dinitrile.
  • the solvent is an organic sulfur-including solvent.
  • the solvent is a combination of an organic sulfur-including solvent and another aprotic solvent.
  • a catholyte which includes a nitrile or dinitrile solvent and a lithium salt.
  • the solvent in the catholyte is selected from the group consisting of from acetonitrile, butyronitrile, benzonitrile, glutaronitrile, hexanenitrile, fluoroacetonitrile, nitroacetonitrile, ethoxyacetonitrile, methoxyacetonitrile, pentanenitrile, propanenitrile, succinonitrile, adiponitrile, iso-butyronitrile, malononitrile and combinations thereof.
  • the catholyte solvent is fluoromethyl ethylene carbonate, ethyl nitroacetate, N-Methylpyrrolidone, ⁇ -butyrolactone, ethyl methyl sulfone, dimethyl sulfone, sulfolane, allyl methyl sulfone, butadiene sulfone, butyl sulfone, methyl methanesulfonate, dimethyl sulfite, dimethyl sulfoxide, dimethylsulfate, 3-methyl-2-oxazolidinone, fluorinated cyclic carbonate, methylene methane disulfonate, methyl cyanoacetate.
  • the solvent is acetonitrile. In certain examples, the solvent is butyronitrile. In certain examples, the solvent is glutaronitrile. In certain examples, the solvent is hexanenitrile. In certain examples, the solvent is fluoroacetonitrile. In certain examples, the solvent is nitroacetonitrile. In certain examples, the solvent is iso-butyronitrile. In certain examples, the solvent is ethoxyacetonitrile. In certain examples, the solvent is pentanenitrile. In certain examples, the solvent is propanenitrile. In certain examples, the solvent is succinonitrile. In certain examples, the solvent is adiponitrile. In certain examples, the solvent is malononitrile.
  • the solvent is benzonitrile. In certain examples, the solvent is methoxyacetonitrile. In certain examples, the solvent is a combination of succinonitrile and adiponitrile. In certain examples, the solvent is a combination of succinonitrile and glutaronitrile.
  • the electrochemical cell set forth herein includes a dinitrile solvent which includes a dinitrile represented by Formula (I):
  • R 1 , R 2 , R 3 , and R 4 are, independently in each instance, —H or —CN.
  • R 1 , R 2 , R 3 , and R 4 are, independently in each instance, —H or —NO 2 .
  • R 1 , R 2 , R 3 , and R 4 are, independently in each instance, —H or —CO 2 .
  • R 1 , R 2 , R 3 , and R 4 are, independently in each instance, —H or —SO 4 . In some of the examples herein, R 1 , R 2 , R 3 , and R 4 are, independently in each instance, —H or —SO 3 . In some of the examples herein, R 1 , R 2 , R 3 , and R 4 are, independently in each instance, —H or —SO 2 .
  • R 1 , R 2 , R 3 , and R 4 are, independently in each instance, —H or —CH 2 —SO 3 .
  • R 1 , R 2 , R 3 , and R 4 are, independently in each instance, —H or —CHF—SO 3 .
  • R 1 , R 2 , R 3 , and R 4 are, independently in each instance, —H or —CF 2 —SO 3 .
  • R 1 , R 2 , R 3 , and R 4 are, independently in each instance, —H or —F.
  • R 1 , R 2 , R 3 , and R 4 are, independently in each instance, —H or —Cl.
  • R 1 , R 2 , R 3 , and R 4 are, independently in each instance, —H or —Br.
  • R 1 , R 2 , R 3 , and R 4 are, independently in each instance, —H or —I.
  • the catholyte solvent includes a member selected from the group consisting of:
  • the solvent is a combination of succinonitrile and adiponitrile. In certain examples, the solvent is a combination of succinonitrile and glutaronitrile.
  • the catholyte solvent includes an organic sulfur-including solvent.
  • the organic sulfur-including solvent is selected from the group consisting of ethyl methyl sulfone, dimethyl sulfone, sulfolane, allyl methyl sulfone, butadiene sulfone, butyl sulfone, methyl methanesulfonate, and dimethyl sulfite.
  • the lithium salt is selected from LiPF 6 , LiBOB, LiTFSi, LiFSI, LiAsF 6 , LiClO 4 , LiI, LiBF 4 , and a combination thereof.
  • the lithium salt is LiPF 6 , In certain examples, the lithium salt is LiBOB. In certain examples, the lithium salt is LiTFSi. In certain examples, the lithium salt is LiBF 4 . In certain examples, the lithium salt is LiClO 4 . In certain examples, the lithium salt is LiFSI. In certain examples, the lithium salt is LiAsF 6 . In certain examples, the lithium salt is LiClO 4 . In certain examples, the lithium salt is LiI. In certain examples, the lithium salt is LiBF 4 .
  • the catholyte is chemically stable when in contact with a solid separator.
  • the electrochemical cell further includes a bonding layer which includes a solvent selected from ethylene carbonate (EC), diethylene carbonate, diethyl carbonate, dimethyl carbonate (DMC), ethyl-methyl carbonate (EMC), tetrahydrofuran (THF), ⁇ -Butyrolactone (GBL), fluoroethylene carbonate (FEC), fluoromethyl ethylene carbonate (FMEC), trifluoroethyl methyl carbonate (F-EMC), fluorinated 3-(1,1,2,2-tetrafluoroethoxy)-1,1,2,2-tetrafluoropropane (i.e., 1,1,2,2-tetrafluoro-3-(1,1,2,2-tetrafluoroethoxy)propane (F-EPE)), fluorinated cyclic carbonate (F-AEC), propylene carbonate (PC), dioxolane, acetonitrile (ACN), succinonitrile, adip
  • the solvent is ethylene carbonate (EC). In some examples, the solvent is diethylene carbonate. In some examples, the solvent is dimethyl carbonate (DMC). In some examples, the solvent is ethyl-methyl carbonate (EMC). In some examples, the solvent is tetrahydrofuran (THF). In some examples, the solvent is ⁇ -Butyrolactone (GBL). In some examples, the solvent is fluoroethylene carbonate (FEC). In some examples, the solvent is fluoromethyl ethylene carbonate (FMEC). In some examples, the solvent is trifluoroethyl methyl carbonate (F-EMC).
  • EC ethylene carbonate
  • DMC dimethyl carbonate
  • EMC ethyl-methyl carbonate
  • THF tetrahydrofuran
  • GBL ⁇ -Butyrolactone
  • the solvent is fluoroethylene carbonate (FEC). In some examples, the solvent is fluoromethyl ethylene carbonate (FMEC). In some examples, the solvent is trifluoro
  • the solvent is fluorinated 3-(1,1,2,2-tetrafluoroethoxy)-1,1,2,2-tetrafluoropropane (i.e., 1,1,2,2-tetrafluoro-3-(1,1,2,2-tetrafluoroethoxy)propane (F-EPE)).
  • the solvent is fluorinated cyclic carbonate (F-AEC).
  • the solvent is propylene carbonate (PC).
  • the solvent is dioxolane.
  • the solvent is acetonitrile (ACN).
  • the solvent is succinonitrile.
  • the solvent is adiponitrile/hexanedinitrile.
  • the solvent is acetophenone. In some examples, the solvent is isophorone. In some examples, the solvent is benzonitrile. In some examples, the solvent is dimethyl sulfate. In some examples, the solvent is dimethyl sulfoxide (DMSO). In some examples, the solvent is ethyl acetate. In some examples, the solvent is methyl butyrate. In some examples, the solvent is dimethyl ether (DME). In some examples, the solvent is diethyl ether. In some examples, the solvent is dioxolane. In some examples, the solvent is glutaronitrile. In some examples, the solvent is gamma butyrolactone. In some examples, the solvent is a combination of any solvents mentioned above. This bonding layer may be used to adhere or bond the cathode to the solid separator.
  • DMSO dimethyl sulfoxide
  • DME dimethyl ether
  • the solvent diethyl ether.
  • the solvent is dioxolane.
  • the solvent is
  • the electrochemical cell further includes a bonding layer which includes a lithium salt in the bonding layer is selected from LiPF 6 , LiBOB, LFTSi, or combinations thereof.
  • the lithium salt in the bonding layer is LiPF 6 at a concentration of 0.5 M to 2 M.
  • the lithium salt in the bonding layer is LiTFSI at a concentration of 0.5 M to 2 M.
  • the catholyte solvent is a solvent having a permittivity of greater than 30. In certain of these examples, the catholyte solvent is a dinitrile-containing solvent.
  • the catholyte solvent is a solvent having a viscosity of greater than 0.01 cP and less than 10 cP at 25° C.
  • the catholyte solvent is a solvent having a flash point of greater than 50° C. and less than 400° C.
  • the catholyte solvent is a solvent having a melting point higher than ⁇ 50° C. and lower than 30° C.
  • the catholyte solvent is a solvent having a boiling point of greater than 80° C.
  • the catholyte solvent is a solvent having a HOMO level of more than 7.2 eV below the vacuum level as calculated by DFT (density fuctional theory) with a B3LYP (Becke, 3-parameter, Lee-Yang-Parr) exchange-correlation functional and 6-311++G** basis set.
  • the HOMO level is more than 7.8 eV below the vacuum level as calculated by DFT with a B3LYP exchange-correlation functional and 6-311++G** basis set.
  • the HOMO level is more than 8.2 eV below the vacuum level as calculated by DFT with a B3LYP exchange-correlation functional and 6-311++G** basis set.
  • the catholyte solvent is a solvent is polar and aprotic.
  • the catholyte has a lithium transference number of greater than 0.2.
  • the catholyte has a total ionic conductivity of greater than 1e-4 S/cm at 25° C.
  • the catholyte solvent has a vapor pressure of lower than 2 Torr at 20° C. In some of the examples herein, the catholyte solvent has a vapor pressure of lower than 0.2 Torr at 20° C. In some of the examples herein, the catholyte solvent has a vapor pressure of lower than 2e-2 Torr at 20° C.
  • the catholyte solvent has a boiling point of greater than 80° C.
  • the catholyte solvent has a boiling point of greater than 250° C.
  • the catholyte solvent has a viscosity of less than 10 centipoise (cP) at 25° C.
  • the catholyte further comprises a carbonate solvent in addition to the nitrile or dinitrile solvent.
  • the catholyte further comprises a solvent selected from ethylene carbonate (EC), diethylene carbonate, diethyl carbonate, dimethyl carbonate (DMC), ethyl-methyl carbonate (EMC), tetrahydrofuran (THF), ⁇ -Butyrolactone (GBL), fluoroethylene carbonate (FEC), fluoromethyl ethylene carbonate (FMEC), trifluoroethyl methyl carbonate (F-EMC), fluorinated 3-(1,1,2,2-tetrafluoroethoxy)-1,1,2,2-tetrafluoropropane/1,1,2,2-tetrafluoro-3-(1,1,2,2-tetrafluoroethoxy)propane (F-EPE), fluorinated cyclic carbonate (F-AEC), propylene carbonate (PC), dioxolane
  • EC ethylene carbonate
  • the catholyte further comprises a carbonate solvent in addition to the organic sulfur-including solvent.
  • the catholyte comprises organic sulfur-including solvent and ethylene carbonate in a ratio of about 1:9, 2:8, 3:7, 4:6, 5:5, 6:4, 7:3, 8:2, or 9:1.
  • the catholyte solvent is stable up to 4.7V v. Lithium. In some of the examples herein, the catholyte solvent is stable up to 4.5V v. Lithium. In some of the examples herein, the catholyte solvent is stable up to 4.4V v. Lithium. In some examples herein, the catholyte solvent is stable up to 4.2V v. Lithium.
  • the catholyte solvent is stable down to 1.5V.
  • the catholyte solvent includes a nitrile represented by Formula (I):
  • R 1 , R 2 , R 3 , and R 4 are, independently in each instance, —H or —CN.
  • R 1 , R 2 , R 3 , and R 4 are, independently in each instance, —H or —NO 2 .
  • R 1 , R 2 , R 3 , and R 4 are, independently in each instance, —H or —CO 2 .
  • R 1 , R 2 , R 3 , and R 4 are, independently in each instance, —H or —SO 4 . In some of the examples herein, R 1 , R 2 , R 3 , and R 4 are, independently in each instance, —H or —SO 3 . In some of the examples herein, R 1 , R 2 , R 3 , and R 4 are, independently in each instance, —H or —SO 2 .
  • R 1 , R 2 , R 3 , and R 4 are, independently in each instance, —H or —CH 2 —SO 3 .
  • R 1 , R 2 , R 3 , and R 4 are, independently in each instance, —H or —CHF—SO 3 .
  • R 1 , R 2 , R 3 , and R 4 are, independently in each instance, —H or —CF 2 —SO 3 .
  • R 1 , R 2 , R 3 , and R 4 are, independently in each instance, —H or —F.
  • R 1 , R 2 , R 3 , and R 4 are, independently in each instance, —H or —Cl.
  • R 1 , R 2 , R 3 , and R 4 are, independently in each instance, —H or —Br.
  • R 1 , R 2 , R 3 , and R 4 are, independently in each instance, —H or —I.
  • subscript m is an integer from 1 to 1000. In some of the examples, subscript m is an integer from 1 to 100. In some of the examples, subscript m is an integer from 1 to 10. In some of the examples, subscript m is an integer from 1 to 5. In some of the examples, subscript m is an integer from 1 to 4. In some of the examples, subscript m is an integer from 1 to 3. In some of the examples, subscript m is an integer from 1 to 2. In some of the examples, subscript m is 1.
  • subscript m is 1. In certain other examples, subscript m is 2. In certain other examples, subscript m is 3. In certain other examples, subscript m is 4. In certain other examples, subscript m is 5. In certain other examples, subscript m is 6. In certain other examples, subscript m is 7. In certain other examples, subscript m is 8. In certain other examples, subscript m is 9. In certain other examples, subscript m is 10. In certain other examples, subscript m is 11. In certain other examples, subscript m is 12. In certain other examples, subscript m is 13. In certain other examples, subscript m is 14. In certain other examples, subscript m is 15. In certain other examples, subscript m is 16. In certain other examples, subscript m is 17. In certain other examples, subscript m is 18. In certain other examples, subscript m is 19. In certain other examples, subscript m is 20.
  • the catholyte includes a solvent selected from the group consisting of
  • the solvent includes both succinonitrile and glutaronitrile. In other examples, the solvent includes succinonitrile and adiponitrile.
  • the dinitrile of Formula I has a total ionic conductivity of greater than 1e-4 S/cm at room temperature.
  • the dinitrile is malononitrile, succinonitrile, glutaronitrile, hexanedinitrile (adipodinitrile), sebaconitrile, subernitrile, pimelonitrile, and dodecanedinitrile, phthalonitrile or cis/trans-1,2-dicyanocyclohexane, or combinations thereof.
  • the lithium salt is selected from LiPF 6 , LiBH 4 , LiBOB, LiBETI, LiTFSi, LiBF 4 , LiClO 4 , LiFSI, LiAsF 6 , LiClO 4 , LiI, LiBF 4 , and combination thereof.
  • the lithium salt is selected from LiPF 6 , LiBH 4 , LiBOB, LiBETI, LiBF 4 , LiAsF 6 , LIFSI, LiTFSI, LiClO 4 , and combinations thereof.
  • the lithium salt is present in the dinitrile solvent at a concentration of about 5-20 mol %.
  • a lithium salt is present in the dinitrile solvent at a concentration of about 12 mol %.
  • the catholyte further comprises a carbonate solvent.
  • the catholyte comprises LiBF 4 , LiCF 3 SO 3 , LiN(CF 3 SO 2 ) 2 , or a combination thereof.
  • the catholyte solvent is a combination as follows:
  • coefficients X, Y, and Z refer to the respective molar amounts of each of acetonitrile, succinonitrile, and glutaronitrile. In some examples, X is 0, Y is 0.87 and Z is 0.13.
  • the catholyte further includes LiBF 4 or LiN(CF 3 SO 2 ) 2 .
  • the catholyte further includes an additives such as VC (vinylene carbonate), VEC (vinyl ethylene carbonate), succinic anhydride, PES (prop-1-ene, 1-3 sultone), tris(trimethylsilyl) phosphite, ethylene sulfate, PBF, TMS (1,3-propylene sulfate), methylene methanedisulfonate (MMDS), lithium nitrate, propylene sulfate, trimethoxyboroxine, FEC, combinations thereof, and the like.
  • VC vinyllene carbonate
  • VEC vinyl ethylene carbonate
  • succinic anhydride PES (prop-1-ene, 1-3 sultone)
  • PES prop-1-ene, 1-3 sultone
  • tris(trimethylsilyl) phosphite ethylene sulfate
  • PBF TMS (1,3-propylene sulfate
  • MMDS methylene
  • the catholyte further includes VC.
  • the catholyte further includes VEC.
  • the catholyte further includes succinic anhydride.
  • the catholyte further includes PES.
  • the catholyte further includes ethylene sulfate.
  • the catholyte further includes PBF.
  • the catholyte further includes TMS.
  • the catholyte further includes propylene sulfate.
  • the catholyte further includes trimethoxyboroxine.
  • the catholyte further includes MMDS.
  • the catholytes here are paired with, laminated to, adjoined, or bonded to a solid separator.
  • the solid separator is a Li conducting solid-state electrolyte material useful as the separator.
  • Separator materials include those that are stable to lithium metal, including sulfides (Li 2 S—SiS 2 —LiX, Li 2 S—B 2 S 3 —LiX, Li 2 S—P 2 S 5 —LiX, Li 2 S—SnS 2 —LiX, Li 2 S-Al 2 S 3 —LiX, and combinations thereof), borohydrides (LiBH 4 —LiX, LiNH 2 —LiX, LiBH 4 —LiNH 2 —LiX, and combinations thereof), LiPON, Li-stuffed garnet, lithium-rich antiperovskite, or LISICON materials.
  • the separators is not stable in contact with metal lithium.
  • the separator is a perovskit
  • some catholyte solvents herein include polar solvents with nitrile functionalities such as acetonitrile, butyronitrile, benzonitrile, hexanenitrile, fluoroacetonitrile, nitroacetonitrile, ethoxyacetonitrile, pentanenitrile, propanenitrile, iso-butyronitrile, and the like.
  • solvents may also include aprotic liquids with electron withdrawing groups such as fluorine (FEC, F-AEC, F-EPE, F-EMC, TTE).
  • solvents may also include aprotic liquids with a low HOMO level as calculated by density functional theory (DFT).
  • DFT density functional theory
  • solvents may also include MMDS, methyl pivalate, 1,2 dioxane, and sulfolane.
  • the oxidative stability of the dinitrile is related to its HOMO. As the HOMO of the dinitrile decreases, or is a higher (less negative) value, it is easier to oxidize the solvent.
  • the lithium salts may include those known in the art such as, but not limited to, LiPF 6 , LiBOB, LiBETI, LiBF 4 , LiAsF 6 , LiFSI, LiTFSI, LiClO 4 , and combinations thereof.
  • the catholyte comprises 0.57:0.43 glutaronitrile:succinonitrile (mol/mol) and 7 mol % LiBF 4 .
  • the catholyte comprises 0.3:0.7 ethylene carbonate:sulfolane (v/v) and 1 M LiPF 6 .
  • set forth herein is an electrochemical cell which includes a catholyte set forth herein.
  • set forth herein is an electrochemical cell which includes a catholyte set forth herein which includes a dinitrile solvent and a lithium salt.
  • set forth herein is an electrochemical cell which includes a catholyte set forth herein which includes a nitrile solvent and a lithium salt.
  • set forth herein is an electrochemical cell which includes a catholyte set forth herein which includes an organic sulfur-including solvent and a lithium salt.
  • an electrochemical cell which includes a lithium metal negative electrode, a solid separator, and a positive electrode.
  • the positive electrode includes an active material, and a catholyte.
  • the catholyte includes a dinitrile solvent and a lithium salt.
  • the lithium metal negative electrode is a layer laminated to the solid separator, wherein the solid separator is a layer laminated to the positive electrode.
  • the lithium metal negative electrode is laminated to the solid separator, wherein the solid separator is laminated to the positive electrode.
  • the lithium metal negative electrode is formed in situ.
  • solid separator is impermeable to the catholyte.
  • the solid separator is dense enough or the catholyte is viscous enough such that the catholyte does not penetrate through the solid separator.
  • the solid separator protects or encapsulates the lithium metal negative electrode and prevents it from contacting the dinitrile catholyte.
  • the electrochemical cell includes a bonding layer between the positive electrode and the solid separator.
  • the bonding layer comprises a solvent and a lithium salt.
  • the solvent in the bonding layer is selected from the group consisting of ethylene carbonate, methylene carbonate, methyl ethyl carbonate, diethylene carbonate.
  • the electrochemical cell includes a lithium salt selected from LiPF 6 , LiBOB, LiTFSi, LiBF 4 , LiClO 4 , LiAsF 6 , LiFSI, LiClO 4 , Li, and a combination thereof.
  • the bonding layer further comprises a polymer selected from the group consisting of polyacrylonitrile (PAN), polypropylene, polyethylene oxide (PEO), polymethyl methacrylate (PMMA), polyvinyl chloride (PVC), polyvinyl pyrrolidone (PVP), polyethylene oxide poly(allyl glycidyl ether) PEO-AGE, polyethylene oxide 2-methoxyethoxy)ethyl glycidyl ether (PEO-MEEGE), polyethylene oxide 2-methoxyethoxy)ethyl glycidyl poly(allyl glycidyl ether) (PEO-MEEGE-AGE), polysiloxane, polyvinylidene fluoride (PVdF), polyvinylidene fluoride hexafluoropropylene (PVdF-HFP), and rubbers such as ethylene propylene (EPR), nitrile rubber (NPR), styrene-butad
  • the polymer in the bonding layer is polyacrylonitrile (PAN) or polyvinylidene fluoride hexafluoropropylene (PVdF-HFP).
  • the polymer in the bonding layer is selected from the group consisting of PAN, PVdF-HFP, PVDF-HFP and PAN, PMMA, PVC, PVP, PEO, and combinations thereof.
  • the polymer is polyacrylonitrile (PAN).
  • the polymer is polypropylene.
  • the polymer is polyethylene oxide (PEO).
  • the polymer is polymethyl methacrylate (PMMA).
  • the polymer is polyvinyl chloride (PVC).
  • the polymer is polyvinyl pyrrolidone (PVP).
  • the polymer is polyethylene oxide poly(allyl glycidyl ether) PEO-AGE.
  • the polymer is polyethylene oxide 2-methoxyethoxy)ethyl glycidyl ether (PEO-MEEGE).
  • the polymer is polyethylene oxide 2-methoxyethoxy)ethyl glycidyl poly(allyl glycidyl ether) (PEO-MEEGE-AGE).
  • the polymer is polysiloxane.
  • the polymer is polyvinylidene fluoride (PVDF).
  • the polymer is polyvinylidene fluoride hexafluoropropylene (PVdF-HFP).
  • the polymer is a rubber such as ethylene propylene (EPR), nitrile rubber (NPR), styrene-butadiene-rubber (SBR), polybutadiene polymer, polybutadiene rubber (PB), polyisobutadiene rubber (PIB), polyisoprene rubber (PI), polychloroprene rubber (CR), acrylonitrile-butadiene rubber (NBR), and polyethyl acrylate (PEA).
  • the polymer is polyethylene (e.g., low density linear polyethylene).
  • the polymer is a combination of any polymers mentioned above.
  • the solvent in the bonding layer is selected from ethylene carbonate (EC), diethylene carbonate, diethyl carbonate, dimethyl carbonate (DMC), ethyl-methyl carbonate (EMC), tetrahydrofuran (THF), ⁇ -Butyrolactone (GBL), fluoroethylene carbonate (FEC), fluoromethyl ethylene carbonate (FMEC), trifluoroethyl methyl carbonate (F-EMC), fluorinated 3-(1,1,2,2-tetrafluoroethoxy)-1,1,2,2-tetrafluoropropane/1,1,2,2-tetrafluoro-3-(1,1,2,2-tetrafluoroethoxy)propane (F-EPE), fluorinated cyclic carbonate (F-AEC), propylene carbonate (PC), dioxolane, acetonitrile (ACN), succinonitrile, adip
  • the solvent in the bonding layer is a 1:1 w/w mixture of EC:PC.
  • the lithium salt in the bonding layer is selected from LiPF 6 , LiBOB, LFTSi, or combinations thereof.
  • the lithium salt in the bonding layer is LiPF 6 at a concentration of 0.5 M to 2M.
  • the lithium salt in the bonding layer is LiTFSI at a concentration of 0.5 M to 2M.
  • the lithium salt in the bonding layer is present at a concentration from 0.01 M to 10 M.
  • the solid separator is selected from a lithium sulfide, a lithium borohydride, a LiPON, a lithium-stuffed garnet, a lithium-rich antiperovskite, a LISICON, and a combination thereof.
  • the solid separator is an oxide selected from a lithium-stuffed garnet characterized by the formula Li x La y Zr z O t .qAl 2 O 3 , wherein 4 ⁇ x ⁇ 10, 1 ⁇ y ⁇ 4, 1 ⁇ z ⁇ 3, 6 ⁇ t ⁇ 14, 0 ⁇ q ⁇ 1.
  • the solid separator is a lithium-stuffed garnet doped with Al, Nb, Ga, and/or Ta.
  • the solid separator is a lithium-stuffed garnet characterized by Li a La b Zr c Al d Me′′ e O f , wherein 5 ⁇ a ⁇ 8.5; 2 ⁇ b ⁇ 4; 0 ⁇ c ⁇ 2.5; 0 ⁇ d ⁇ 2; 0 ⁇ e ⁇ 2, and 10 ⁇ f ⁇ 13 and Me′′ is a metal selected from Nb, Ga, Ta, or combinations thereof.
  • the lithium-stuffed garnet is characterized by the formula Li x La y Zr z O t .0.11(Al 2 O 3 ) or Li x La y Zr z O t .(Al 2 O 3 ), wherein 5 ⁇ x ⁇ 8.5.
  • the solid separator is a sulfide or sulfide-halide is selected from LPSI, LSS, SLOPS, LSTPS, SLOBS, and LATS.
  • the separator is a sulfide or sulfide-halide is selected from LiBHI, LiBNHI, LiBHCl, LiBNHCl, LiBHBr, LiBNHBr, and combinations thereof.
  • the solid separator is a thin film.
  • the solid separator is a monolith.
  • the solid separator is a composite of a polymer and a solid electrolyte.
  • the catholyte solvent(s) is a solvent having a permittivity of greater than 30.
  • the catholyte solvent(s) is a solvent having a viscosity of less than 10 cP at 25° C.
  • the catholyte solvent(s) is a solvent having a flash point of greater than 50° C.
  • the catholyte solvent(s) is a solvent having a melting point of lower than 30° C.
  • the catholyte solvent(s) is a solvent having a boiling point of greater than 80° C.
  • the catholyte solvent(s) is a solvent having a HOMO level of more than 7.2 eV below the vacuum level.
  • the catholyte solvent(s) is polar and aprotic.
  • the nitrile solvent is selected from acetonitrile, butyronitrile, benzonitrile, hexanenitrile, fluoroacetonitrile, nitroacetonitrile, malononitrile, ethoxyacetonitrile, pentanenitrile, propanenitrile, and iso-butyronitrile.
  • the dinitrile solvent comprises a member selected from the group consisting of fluoroethylene carbonate (FEC), fluoromethyl ethylene carbonate (FMEC), trifluoroethyl methyl carbonate (F-EMC), fluorinated 3-(1,1,2,2-tetrafluoroethoxy)-1,1,2,2-tetrafluoropropane (i.e., 1,1,2,2-tetrafluoro-3-(1,1,2,2-tetrafluoroethoxy)propane (F-EPE)), fluorinated cyclic carbonate (F-AEC), and TTE.
  • the dinitrile solvent comprises a member selected from the group consisting of MMDS, methyl pivalate, 1,2 dioxane, sulfolane, and combinations thereof.
  • the catholyte has a lithium transference number of greater than 0.2.
  • the catholyte has a total ionic conductivity of greater than 1e-4 S/cm at 25° C.
  • the catholyte solvent has a vapor pressure of lower than 2e-2 Torr at 20° C., or lower than 0.2 Torr at 20° C., or lower than 2 Torr at 20° C.
  • the catholyte solvent has a boiling point of greater than 80° C.
  • the catholyte solvent has a boiling point of greater than 250° C.
  • the catholyte solvent has a viscosity of less than 10 centipoise (cP) at 25° C.
  • the catholyte further comprises a carbonate solvent.
  • the catholyte further comprises a solvent selected from ethylene carbonate (EC), diethylene carbonate, diethyl carbonate, dimethyl carbonate (DMC), ethyl-methyl carbonate (EMC), tetrahydrofuran (THF), ⁇ -Butyrolactone (GBL), fluoroethylene carbonate (FEC), fluoromethyl ethylene carbonate (FMEC), trifluoroethyl methyl carbonate (F-EMC), fluorinated 3-(1,1,2,2-tetrafluoroethoxy)-1,1,2,2-tetrafluoropropane/1,1,2,2-Tetrafluoro-3-(1,1,2,2-tetrafluoroethoxy)propane (F-EPE), fluorinated cyclic carbonate (F-AEC), propylene carbonate (PC), dioxolane, acetonitrile (ACN), succinonitrile
  • the catholyte solvent is stable up to 4.7V v. Lithium. In some examples, the catholyte solvent is stable up to 4.5V v. Lithium. In some examples, the catholyte solvent is stable up to 4.4V v. Lithium.
  • the catholyte solvent is stable towards the solid separator.
  • the catholyte solvent is stable down to 1.5V.
  • the dinitrile solvent is stable up to 4.7V v. Lithium.
  • the dinitrile solvent is stable towards the solid separator.
  • the dinitrile solvent is stable down to 1.5V.
  • the dinitrile of Formula I has a total ionic conductivity of greater than 1e-4 S/cm at room temperature.
  • the electrochemical cell has a cyclability wherein greater than 70% of the initial energy remains at cycle 100 when cycled at a C/3 rate at 30° C.
  • the electrochemical cell has a lifetime wherein greater than 70% of the initial energy remains at cycle 100 when cycled at a C/3 rate at 30° C.
  • the electrochemical cell has a rate performance wherein greater than 70% of the initial power capability at 50% state-of-charge (SOC) remains at cycle 100 when cycled at a C/3 rate at 30° C.
  • SOC state-of-charge
  • the electrochemical cell has an oxidation potential wherein greater than 70% of the initial energy remains at cycle 100 when cycled at a C/3 rate at 30° C.
  • the electrochemical cell has an impedance at cycle 100 less than 13% of the initial impedance when cycled at a C/3 rate at 30° C.
  • the dinitrile may be selected from malononitrile, succinonitrile, glutaronitrile, hexanedinitrile/adiponitrile, sebaconitrile, subemitrile, pimelonitrile, and dodecanedinitrile, phthalonitrile or cis/trans-1,2-dicyanocyclohexane, and combinations thereof.
  • the lithium salt may be selected from LiPF 6 , LiBH 4 , LiBOB, LiBETI, LiTFSi, LiClO 4 , LiAsF 6 , LiFSI, LiClO 4 , LiI, LiBF 4 , and combination thereof.
  • the lithium salt may be selected from LiPF 6 , LiBH 4 , LiBOB, LiBETI, LiBF 4 , LiAsF 6 , LIFSI, LiTFSI, LiClO 4 , and combinations thereof.
  • the lithium salt is present in the dinitrile solvent at a concentration of about 5-20 mol %.
  • the lithium salt is present in the dinitrile solvent at a concentration of about 12 mol %.
  • the solid separator is a lithium-stuffed-garnet, an LiBHI, Li 3 N, a lithium-sulfides, a LiPON, a LISON, or a combination thereof.
  • the active material is selected from a nickel manganese cobalt oxide (NMC), a nickel cobalt aluminum oxide (NCA), Li(NiCoAl)O 2 , a lithium cobalt oxide (LCO), a lithium manganese cobalt oxide (LMCO), a lithium nickel manganese cobalt oxide (LMNCO), a lithium nickel manganese oxide (LNMO), Li(NiCoMn)O 2 , LiMn 2 O 4 , LiCoO 2 , LiMn 2-a Ni a O 4 , wherein a is from 0 to 2, or LiMPO 4 , wherein M is Fe, Ni, Co, or Mn.
  • NMC nickel manganese cobalt oxide
  • NCA nickel cobalt aluminum oxide
  • LCO lithium cobalt oxide
  • LMCO lithium manganese cobalt oxide
  • LNCO lithium nickel manganese cobalt oxide
  • LNMO lithium nickel manganese oxide
  • the active material is selected from FeF 2 , NiF 2 , FeO x F 3-2x , FeF 3 , MnF 3 , CoF 3 , CuF 2 materials, alloys thereof, and combinations thereof
  • the catholyte herein further includes a carbonate solvent.
  • the catholyte includes LiBF 4 , LiCF 3 SO 3 , LiN(CF 3 SO 2 ) 2 , or a combination thereof.
  • the dinitrile is a combination as follows:
  • the electrochemical cell herein includes LiBF 4 or LiN(CF 3 SO 2 ) 2 .
  • the electrochemical cell herein includes a solid separator which includes a lithium-stuffed garnet oxide characterized by the formula Li u La v Zr x O y .zAl 2 O 3 , wherein
  • u is selected from 4, 5, 6, 7, and 8; v is selected from 2, 3, and 4; x is selected from 1, 2, and 3; y is selected from 10, 11, 12, 13, and 14; and z is selected from 0.05, 0.1, 0.15, 0.2, 0.25, 0.3, 0.35, 0.4, 0.45, 0.5, 0.55, 0.6, 0.65, 0.7, 0.75, 0.8, 0.85, 0.9, 0.95, and 1.
  • the electrochemical cell herein includes a solid separator which includes a lithium sulfide characterized by one of the following Formula:
  • the electrochemical cell herein includes a solid separator which includes a lithium-stuffed garnet oxide characterized by the formula Li u La v Zr x O y .zTa 2 O 5 , wherein
  • u is selected from 4, 5, 6, 7, 8, 9, and 10; v is selected from 2, 3, and 4; x is selected from 1, 2, and 3; y is selected from 10, 11, 12, 13, and 14; and z is selected from 0, 0.05, 0.1, 0.15, 0.2, 0.25, 0.3, 0.35, 0.4, 0.45, 0.5, 0.55, 0.6, 0.65, 0.7, 0.75, 0.8, 0.85, 0.9, 0.95, and 1.
  • the electrochemical cell herein includes a solid separator which includes a lithium-stuffed garnet oxide characterized by the formula Li u La v Zr x O y .zNb 2 O 5 , wherein
  • u is selected from 4, 5, 6, 7, 8, 9, and 10; v is selected from 2, 3, and 4; x is selected from 1, 2, and 3; y is selected from 10, 11, 12, 13, and 14; and z is selected from 0, 0.05, 0.1, 0.15, 0.2, 0.25, 0.3, 0.35, 0.4, 0.45, 0.5, 0.55, 0.6, 0.65, 0.7, 0.75, 0.8, 0.85, 0.9, 0.95, and 1.
  • the electrochemical cell herein include a solid separator which includes a lithium-stuffed garnet oxide characterized by the formula Li u La v Zr x O y .z Ga 2 O 3 , wherein
  • u is selected from 4, 5, 6, 7, 8, 9, and 10; v is selected from 2, 3, and 4; x is selected from 1, 2, and 3; y is selected from 10, 11, 12, 13, and 14; and z is selected from 0, 0.05, 0.1, 0.15, 0.2, 0.25, 0.3, 0.35, 0.4, 0.45, 0.5, 0.55, 0.6, 0.65, 0.7, 0.75, 0.8, 0.85, 0.9, 0.95, and 1.
  • the electrochemical cell herein includes a solid separator which includes a lithium-stuffed garnet oxide characterized by the formula Li u La v Zr x O y .zTa 2 O 5 bAl 2 O 3 , wherein
  • u is selected from 4, 5, 6, 7, 8, 9, and 10; v is selected from 2, 3, and 4; x is selected from 1, 2, and 3; y is selected from 10, 11, 12, 13, and 14; and z and b are each independently selected from 0, 0.05, 0.1, 0.15, 0.2, 0.25, 0.3, 0.35, 0.4, 0.45, 0.5, 0.55, 0.6, 0.65, 0.7, 0.75, 0.8, 0.85, 0.9, 0.95, and 1.
  • the electrochemical cell herein includes a solid separator which includes a lithium-stuffed garnet oxide characterized by the formula Li u La v Zr x O y .zNb 2 O 5 bAl 2 O 3 , wherein
  • u is selected from 4, 5, 6, 7, 8, 9, and 10; v is selected from 2, 3, and 4; x is selected from 1, 2, and 3; y is selected from 10, 11, 12, 13, and 14; and z and b are each independently selected from 0, 0.05, 0.1, 0.15, 0.2, 0.25, 0.3, 0.35, 0.4, 0.45, 0.5, 0.55, 0.6, 0.65, 0.7, 0.75, 0.8, 0.85, 0.9, 0.95, and 1.
  • the electrochemical cell herein includes a solid separator which includes a lithium-stuffed garnet oxide characterized by the formula Li u La v Zr x O y .z Ga 2 O 3 .bAl 2 O 3 , wherein
  • u is selected from 4, 5, 6, 7, 8, 9, and 10.
  • v is selected from 2, 3, and 4.
  • x is selected from 1, 2, and 3.
  • y is selected from 10, 11, 12, 13, and 14.
  • z and b are each independently selected from 0, 0.05, 0.1, 0.15, 0.2, 0.25, 0.3, 0.35, 0.4, 0.45, 0.5, 0.55, 0.6, 0.65, 0.7, 0.75, 0.8, 0.85, 0.9, 0.95, and 1.
  • the electrochemical cell herein includes a positive electrode in direct contact with a solid electrolyte separator.
  • the electrochemical cell herein includes catholyte which includes an additives such as VC (vinylene carbonate), VEC (vinyl ethylene carbonate), succinic anhydride, PES (prop-1-ene, 1-3 sultone), tris(trimethylsilyl) phosphite, ethylene sulfate, PBF, TMS (1,3-propylene sulfate), propylene sulfate, MMDS, trimethoxyboroxine, FEC, combinations thereof, and the like.
  • VC vinyllene carbonate
  • VEC vinyl ethylene carbonate
  • succinic anhydride PES (prop-1-ene, 1-3 sultone)
  • PES prop-1-ene, 1-3 sultone
  • tris(trimethylsilyl) phosphite ethylene sulfate
  • PBF TMS (1,3-propylene sulfate
  • propylene sulfate MMDS
  • the solid separator of the electrochemical cell is a thin and free standing sintered garnet film, wherein the film thickness is less than 50 ⁇ m and greater than 10 nm, wherein the film comprises a garnet characterized by the formula Li x La 3 Zr 2 O 12 .qAl 2 O 3 , wherein x ranges from 5.5 to 9; and q ranges from 0.05 to 1.0; and wherein the film is not adhered or fixed to a substrate.
  • the molar ratio of Al 2 O 3 :Li x La 3 Zr 2 O 12 is 0.35, 0.5, 0.67 or 1.0.
  • the film has a surface roughness of less than 5 ⁇ m.
  • the garnet has a median grain size of between 0.1 ⁇ m and 10 ⁇ m.
  • the film has an area specific resistance (ASR) of less than 10 ⁇ cm 2 .
  • the film has an area specific resistance (ASR) of less than 10 ⁇ cm 2 at 80° C.
  • the carbon content is less than 5 atomic %.
  • the film thickness is about 49 ⁇ m.
  • the solid separator of the electrochemical cell is a thin film comprising a lithium stuffed garnet and Al 2 O 3 , wherein the lithium-stuffed garnet is characterized by the empirical formula Li x La y Zr z O t , wherein 5.5 ⁇ x ⁇ 6.7, 1.5 ⁇ y ⁇ 4, 1 ⁇ z ⁇ 2, 10 ⁇ t ⁇ 13; and wherein the molar ratio of Al 2 O 3 :gamet is between 0.05 to 0.7; wherein the thin film has a film thickness of about 10 nm to about 100 ⁇ m; and wherein the thin film has grains having a d 50 diameter between 100 nm and 10 ⁇ m.
  • the thin film is characterized by the empirical formula Li x La 3 Zr 2 O 12 .p1 ⁇ 2Al 2 O 3 ; wherein 5.5 ⁇ x ⁇ 6.7 and 0.1 ⁇ p ⁇ 1.4.
  • the molar ratio of Al 2 O 3 :garnet is between 0.25 and 0.45. In some examples, the molar ratio of Al 2 O 3 :garnet is 0.35.
  • the film thickness is less than 50 ⁇ m and greater than 10 nm.
  • the thin film is a thin film monolith. In some examples, the thin film is a sintered thin film monolith. In some examples, the thin film has a density of about 4.5-5.2 g/cm 3 .
  • set forth herein is a method for making a catholyte set forth herein which includes a nitrile solvent and a lithium salt, wherein the method includes providing a nitrile solvent, providing a lithium salt, mixing the dinitrile solvent and the lithium salt to form a mixture, and optionally heating the mixture.
  • the nitrile solvent is a dinitrile solvent.
  • the nitrile solvent comprises or is selected from those solvents described above with respect to the catholyte of the present invention(s).
  • the nitrile solvent has the properties described above with respect to the catholyte of the present invention(s).
  • the lithium salt is selected from those lithium salts described above with respect to the catholyte of the present invention(s).
  • the nitrile solvent further comprises a solvent selected from those described above with respect to the catholyte of the present invention(s).
  • set forth herein is a method for making a catholyte set forth herein which includes an organic sulfur-including solvent and a lithium salt, wherein the method includes providing an organic sulfur-including solvent, providing a lithium salt, mixing the organic sulfur-including solvent and the lithium salt to form a mixture, and optionally heating the mixture.
  • the method includes drying the solvent(s) and/or salts before or after mixing.
  • the drying comprises heating and/or processing the material with a desiccating or absorbing material.
  • set forth herein is a method of using an electrochemical cell, which is set forth herein, or using an electrochemical cell that includes a catholyte, which is set forth herein.
  • the methods include charging the electrochemical cell to a voltage greater than 4.3V.
  • the methods also include discharging the electrochemical cell to a voltage less than 4.3V.
  • the methods herein include charging the battery to a voltage greater than 4.4V. In some examples, the methods herein include charging the battery to a voltage greater than 4.5V. In some examples, the methods herein include charging the battery to a voltage greater than 4.6V. In some examples, the methods herein include charging the battery to a voltage greater than 4.7V. In some examples, the methods herein include charging the battery to a voltage greater than 4.8V. In some examples, the methods herein include charging the battery to a voltage greater than 4.9V. In some examples, the methods herein include charging the battery to a voltage greater than 5.0V. In some examples, the methods herein include charging the battery to a voltage greater than 5.1V.
  • the methods herein include charging the battery to a voltage greater than 5.2V. In some examples, the methods herein include charging the battery to a voltage greater than 5.3V. In some examples, the methods herein include charging the battery to a voltage greater than 5.4V. In some examples, the methods herein include charging the battery to a voltage greater than 5.5V.
  • the methods herein include charging the battery under pressure.
  • the pressure is about 50-300 pounds per square inch (PSI). In some examples, the pressure is about 50 PSI. In some examples, the pressure is about 60 PSI. In some examples, the pressure is about 70 PSI. In some examples, the pressure is about 80 PSI. In some examples, the pressure is about 90 PSI. In some examples, the pressure is about 100 PSI. In some examples, the pressure is about 110 PSI. In some examples, the pressure is about 120 PSI. In some examples, the pressure is about 130 PSI. In some examples, the pressure is about 140 PSI. In some examples, the pressure is about 150 PSI. In some examples, the pressure is about 160 PSI. In some examples, the pressure is about 170 PSI.
  • PSI pounds per square inch
  • the pressure is about 180 PSI. In some examples, the pressure is about 190 PSI. In some examples, the pressure is about 200 PSI. In some examples, the pressure is about 210 PSI. In some examples, the pressure is about 220 PSI. In some examples, the pressure is about 230 PSI. In some examples, the pressure is about 240 PSI. In some examples, the pressure is about 250 PSI. In some examples, the pressure is about 260 PSI. In some examples, the pressure is about 270 PSI. In some examples, the pressure is about 280 PSI. In some examples, the pressure is about 290 PSI. In some examples, the pressure is about 300 PSI.
  • the methods herein include discharging the battery under pressure.
  • the pressure is about 50-300 pounds per square inch (PSI). In some examples, the pressure is about 50 PSI. In some examples, the pressure is about 60 PSI. In some examples, the pressure is about 70 PSI. In some examples, the pressure is about 80 PSI. In some examples, the pressure is about 90 PSI. In some examples, the pressure is about 100 PSI. In some examples, the pressure is about 110 PSI. In some examples, the pressure is about 120 PSI. In some examples, the pressure is about 130 PSI. In some examples, the pressure is about 140 PSI. In some examples, the pressure is about 150 PSI. In some examples, the pressure is about 160 PSI.
  • PSI pounds per square inch
  • the pressure is about 170 PSI. In some examples, the pressure is about 180 PSI. In some examples, the pressure is about 190 PSI. In some examples, the pressure is about 200 PSI. In some examples, the pressure is about 210 PSI. In some examples, the pressure is about 220 PSI. In some examples, the pressure is about 230 PSI. In some examples, the pressure is about 240 PSI. In some examples, the pressure is about 250 PSI. In some examples, the pressure is about 260 PSI. In some examples, the pressure is about 270 PSI. In some examples, the pressure is about 280 PSI. In some examples, the pressure is about 290 PSI. In some examples, the pressure is about 300 PSI.
  • set forth herein method of storing an electrochemical cell includes providing an electrochemical cell of any one of claims, wherein the an electrochemical cell has greater than 20% state-of-charge (SOC); and storing the battery for at least one day.
  • SOC state-of-charge
  • the storing the battery is for at least two days.
  • the storing the battery is for at least three days.
  • the storing the battery is for at least four days.
  • the storing the battery is for at least five days.
  • the storing the battery is for at least six days.
  • the storing the battery is for at least seven days.
  • the storing the battery is for at least nine days.
  • the storing the battery is for at least ten days.
  • the storing the battery is for at least eleven days.
  • the storing the battery is for at least twelve days.
  • the storing the battery is for at least thirteen days.
  • the storing the battery is for at least fourteen days.
  • the storing the battery is for at least fifteen days.
  • the storing the battery is for at least sixteen days.
  • the storing the battery is for at least seventeen days.
  • the storing the battery is for at least eighteen days.
  • the storing the battery is for at least nineteen days.
  • the storing the battery is for at least twenty days.
  • the storing the battery is for at least twenty-one days.
  • the storing the battery is for at least twenty-two days.
  • the storing the battery is for at least twenty-three days.
  • the storing the battery is for at least twenty-four days.
  • the storing the battery is for at least twenty-five days.
  • the storing the battery is for at least twenty-seven days. [and 28, 29, and 30 days]
  • the storing the battery for at least one day is at a temperature greater than 20° C. In some other examples, the storing the battery for at least one day is at a temperature greater than 40° C.
  • the method further includes charging the battery to a voltage greater than 4.3V v. Li.
  • a Biologic VMP3 was used to record conductivity.
  • An electrochemical cell was constructed with blocking electrodes.
  • a catholyte material was made as a gel and was used to fill the porosity of a porous separator such as a Celgard membrane or glass fiber separator.
  • a mass loss on drying tool such as an Arizona Instruments Computrac Max 5000XL #1 was used. Electrochemical cycling was performed with Arbin BT-G or BT-2043.
  • GITT Globalvanostatic intermittent titration technique
  • One electrochemical cell included a cathode, layered with a gel electrolyte (i.e., catholyte), which was layered with a solid garnet separator, and to which the opposite side of the solid garnet separator was layered with Li metal by evaporation.
  • the cell was maintained at a pressure of about 50-300 psi.
  • the gel electrolyte included ethylene carbonate:ethyl-methyl-carbonate (EC:EMC) in a 3:7 w/w ratio+1M LiPF 6 at 2 w/w FEC.
  • the solid garnet separator is a pellet cell which can be prepared according to the methods disclosed in U.S. Provisional Application No. 62/544,724 filed Aug. 11, 2017, which is incorporated by reference herein in its entirety.
  • a second electrochemical cell included a cathode, layered with a electrolyte (i.e., catholyte), which was layered with a solid garnet separator, and to which the opposite side of the solid garnet separator was layered with Li metal by evaporation.
  • the cell was maintained at a pressure of about 50-300 psi.
  • the electrolyte included succinonitrile and 12 mol % LiBF 4 .
  • the two cells described in this Example were stored at high voltage (4.6V) at 45° C. and monitored for four weeks. After each week, each cell was discharged to measure the self-discharge, followed by a full charge-discharge at C/10, 2.7-4.5V, with 30 min pulses followed by 1 min rests to measure the ASR.
  • This Example compares electrolyte performance when the coin cell cap, on the anode side, has been compromised.
  • a hole was drilled into the coin cell cap, on the anode side.
  • the cell included a cathode, layered with a electrolyte (i.e., catholyte), which was layered with a solid garnet separator, and to which the opposite side of the solid garnet separator was layered with Li metal by evaporation.
  • the cell was maintained at a pressure of about 50-300 psi.
  • the electrolyte included ethylene carbonate:ethyl-methyl-carbonate (EC:EMC) in a 3:7 w/w ratio+1M LiPF 6 at 2 w/w FEC.
  • EC:EMC ethylene carbonate:ethyl-methyl-carbonate
  • the cell included a cathode, layered with a electrolyte (i.e., catholyte),which was layered with a solid garnet separator, and to which the opposite side of the solid garnet separator was layered with Li metal by evaporation.
  • the cell was maintained at a pressure of about 50-300 psi.
  • the electrolyte included succinonitrile and 12 mol % LiBF 4 .
  • Both of the two cell batches in this Example were tested in a glovebox at 45° C. within an hour of the crimping. 1/16 inch holes were pre-drilled in the anode cap, which was then used in a standard cell build. Within an hour after crimping, the cells were put on test in a argon-filled glove box at 45° C. The test included a GITT charge-discharge protocol of a pulsed C/10 charge followed by a pulsed C/3 discharge.
  • This Example compares the storage stability of two types of electrochemical cells.
  • One electrochemical cell included a cathode, layered with a gel electrolyte (i.e., catholyte), which was layered with a solid garnet separator, and to which the opposite side of the solid garnet separator was layered with Li metal by evaporation.
  • the cell was maintained at a pressure of about 50-300 psi.
  • the cell included a seal around the garnet to isolate the cathode/catholyte from the lithium anode.
  • the gel electrolyte included ethylene carbonate:ethyl-methyl-carbonate (EC:EMC) in a 3:7 w/w ratio+1M LiPF 6 at 2 w/w FEC.
  • EC:EMC ethylene carbonate:ethyl-methyl-carbonate
  • a second electrochemical cell included a cathode, layered with a electrolyte (i.e., catholyte),which was layered with a solid garnet separator, and to which the opposite side of the solid garnet separator was layered with Li metal by evaporation.
  • the cell was maintained at a pressure of about 50-300 psi.
  • the electrolyte included succinonitrile and 12 mol % LiBF 4 .
  • Both of the two cells were monitored for impedance growth during cycling.
  • the electrochemical cell having the succinonitrile solvent in the cathode electrolyte was observed to have a lower impedance growth, over 50 cycles, when compared to the electrochemical cell having the carbonate solvent in the cathode electrolyte.
  • the electrochemical cell having the succinonitrile solvent therefore had a greater power and energy capability than the electrochemical cell having the carbonate solvent in the cathode electrolyte.
  • Example herein shows that the selected dinitriles are much less prone to solvent evaporation as compared to carbonates.
  • Full cells were prepared with two different catholytes: in one case, ethylene carbonate with 2M LiPF 6 , and in the second case, sulfolane with 2M LiPF 6 .
  • Each full cell device was stored at 45° C. after charging to 4.5V.
  • Each week the device was discharged, and the measured discharge capacity that remained after the week of high temperature storage is called the self-discharged capacity. Then the device was charged and discharged, and the difference between the original capacity and the newly measured reversible capacity provided the irreversible capacity loss after high voltage storage.
  • the device was charged to 4.5V and stored for another week before repeating the discharge tests.
  • the cells retained both self-discharged capacity and reversible capacity for four weeks of storage at 4.5V.
  • cathode is prepared with mass fraction 0.91 NMC, 0.010 Ketjenblack EC-600JD, 0.050 Kynar Powerflex LBG PVDF 12C9073, 0.030 SuperC65; mixed with NMP (N-mthyl-2-pyrolidone) and degassed, then cast on carbon-coated aluminum foil, dried at 120° C. under vacuum, and calendered. There was no bonding layer. Separator was 120 ⁇ m thick.
  • ASR growth wherein the cell was prepared with sulfolane and ethylene carbonate (3:7 v/v)+2M LiPF 6 was a lot smaller than a cell prepared with ethyl-methyl carbonate, ethylene carbonate (3:7 v/v)+1M LiPF 6 .
  • the data was obtained for 10 cycles, C/3 pulses, from 2.7-4.2 V at 45° C.
  • the cathode was NMC, and the separator was solid-state separator material.
  • a cell was able to charge and discharge energy for 500 cycles with minimal gain in ASR.
  • the electrochemical performance for electrochemical cells having a nitrile catholyte is surprisingly improved when compared to electrochemical cells having a carbonate catholyte.
  • high temperature physical stability, high voltage stability, elevated temperature power capability, and cycle life are much better for electrochemical cells having a nitrile catholyte than they are for electrochemical cells having a carbonate catholyte.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Condensed Matter Physics & Semiconductors (AREA)
  • General Physics & Mathematics (AREA)
  • Secondary Cells (AREA)

Abstract

Provided herein are electrochemical cells having a solid separator, a lithium metal anode, and a positive electrode catholyte wherein the electrochemical cell includes a nitrile, dinitrile, or organic sulfur-including solvent and a lithium salt dissolved therein. Also set forth are methods of making and using these electrochemical cells.

Description

CROSS-REFERENCE TO RELATED APPLICATIONS
This application is a National Stage Filing under 35 U.S.C. § 371 of International Patent Application No. PCT/US2017/049218, filed Aug. 29, 2017, which claims the benefit of priority to U.S. Provisional Patent Application No. 62/380,942, filed Aug. 29, 2016, the entire contents of each of which are herein incorporated by reference in their entirety for purposes.
FIELD
The present disclosure sets forth high voltage-stable electrolytes, such as dinitrile solvents and mixtures of dinitrile solvents and nitrile solvents, and organic sulfur-including solvents which include lithium salts, electrochemical cells and devices which include these electrolytes, and methods of making and using the same.
BACKGROUND
Conventional lithium rechargeable batteries use a porous polyolefin separator which is soaked with liquid electrolytes. This separator electrically insulates the positive and negative electrodes of the battery but remains conductive towards Li+ ions. This conventional battery architecture relies on carbonate-based organic solvents, which suffer from flammability and leakage problems, to achieve commercially relevant ion-conductivity, cycle life, and shelf life metrics. Carbonates also have a limited (i.e., narrow) voltage stability window and are particularly unstable when stored at high voltages. Most importantly, carbonate solvents are not chemically compatible with all lithium metal negative electrodes.
Some researchers have attempted to use nitrile solvents in place of carbonate solvents. See, for example, Abu-Lebdeh, Y., et al., Journal of Power Sources 189 (2009) 576-579; Abu-Lebdeh, Y., et al., Journal of The Electrochemical Society, 156 (1) A60-A65 (2009); Long, S. et al., Solid State Ionics 161 (2003) 105-112; Geirhos, K. et al., The Journal of Chemical Physics, 143, 081101 (2015); Zachariah, M., et al. J. Phys. Chem. C 2015, 119, 27298-27306; and Alarco, P-J., et al., nature materials (3), July, 2004. However, these prior uses of nitrile solvents suffered from instability with low voltage anodes such as graphite or lithium metal which are used in high energy batteries. This was due in part because nitrile solvents are not able to form a passivating solid-electrolyte-interface (SEI) on low voltage anodes, such as lithium metal. To date, nitrile solvents have not, which makes nitrile solvents unusable in high energy (i.e., high voltage) batteries. As a result, these graphite and lithium metal anodes typically have, prior to the instant disclosure, required a carbonate co-solvent for the electrolyte.
Some researchers have electrospun or polymerized nitrile-based materials for battery applications, for example Zhou D., et al. (2015) In Situ Synthesis of a Hierarchical All-Solid-State Electrolyte Based on Nitrile Materials for High-Performance Lithium-Ion Batteries. Adv. Energy Mater., 5: 1500353. doi: 10.1002/aenm.201500353. However, the impedance observed in these electrospun or polymerized nitrile-based materials high, the low temperature power capability of the batteries which used these electrospun or polymerized nitrile-based materials is poor, and the electrospun or polymerized nitrile-based materials could not block the formation of lithium dendrites at commercially relevant current densities and commercially relevant throughput amounts of of lithium during electrochemical cycling.
Accordingly, there exists a need for improved electrolytes for rechargeable batteries. Set forth herein are such improved electrolytes as well as other solutions to problems in the relevant field.
SUMMARY
In one embodiment, set forth herein is an electrochemical cell which includes: a lithium metal negative electrode;
a solid separator; and
a positive electrode,
wherein the positive electrode includes an active material and a catholyte,
wherein the catholyte includes a catholyte solvent and a lithium salt, wherein the catholyte solvent comprises a nitrile solvent, a dinitrile solvent, an organic sulfur-including solvent, or a combination thereof.
In a second embodiment, set forth herein is a catholyte including a nitrile solvent and a lithium salt,
    • wherein the nitrile solvent is selected from acetonitrile, butyronitrile, benzonitrile, glutaronitrile, hexanenitrile, fluoroacetonitrile, nitroacetonitrile, malononitrile, ethoxyacetonitrile, methoxyacetonitrile, pentanenitrile, propanenitrile, succinonitrile, adiponitrile, and iso-butyronitrile;
    • wherein the lithium salt is selected from LiPF6, LiBOB, LiTFSi, LiBF4, LiClO4, LiAsF6, LiFSI, LiClO4, LiI, and a combination thereof; and
    • wherein the catholyte is chemically compatible with a solid separator set forth herein.
In a third embodiment, set forth herein is a catholyte comprising an organic sulfur-including solvent, optionally a co-solvent, and a lithium salt,
    • wherein the organic sulfur-including solvent is selected from ethyl methyl sulfone, dimethyl sulfone, sulfolane, allyl methyl sulfone, butadiene sulfone, butyl sulfone, methyl methanesulfonate, dimethyl sulfite, wherein the co-solvent is a carbonate solvent;
    • wherein the lithium salt is selected from LiPF6, LiBOB, LiTFSi, LiBF4, LiClO4, LiAsF6, LiFSI, LiClO4, LiI, and a combination thereof.
In a fourth embodiment, set forth herein is a method of using an electrochemical cell set forth herein, comprising charging the electrochemical cell to a voltage greater than 4.3V.
In a fifth embodiment, set forth herein is a method of storing an electrochemical cell, including providing an electrochemical cell set forth herein, wherein the electrochemical cell has greater than 20% state-of-charge (SOC); and storing the battery for at least one day.
In a sixth embodiment, set forth herein is a method for making a catholyte set forth herein which includes a nitrile solvent and a lithium salt, wherein the method includes providing a nitrile solvent, providing a lithium salt, mixing the nitrile solvent and the lithium salt to form a mixture, and optionally heating the mixture.
In a seventh embodiment, set forth herein is a method for making a catholyte set forth herein which includes an organic sulfur-including solvent and a lithium salt, wherein the method includes providing an organic sulfur-including solvent, providing a lithium salt, mixing the organic sulfur-including solvent and the lithium salt to form a mixture, and optionally heating the mixture.
BRIEF DESCRIPTIONS OF THE DRAWINGS
FIG. 1 shows a schematic of an example of an electrochemical cell having a catholyte in the positive electrode space which includes a dinitrile solvent.
FIG. 2 shows a plot of the median charge ASR-DC (Ω-cm2) for two electrochemical cells, after storage at 4.6 V, and wherein one electrochemical cell includes a catholyte including succinonitrile (SCN) at 12 mol % LiBF4 and wherein the other electrochemical cell includes a catholyte including EC:EMC+1 M LiPF6+2 wt % monofluoroethylene carbonate (FEC). In the figure, circles refer to succinonitrile+12 mol % LiBF4, and triangles refer to EC:EMC+1 M LiPF6+2 wt % FEC. Elyte in FIG. 2 refers to electrolyte. EC refers to ethyl carbonate solvent. EMC refers to ethyl methyl carbonate solvent.
FIG. 3 shows a plot of the median discharge ASR-DC (Ω-cm2) for two electrochemical cells, after storage at 4.6 V, and wherein one electrochemical cell includes a catholyte including succinonitrile (SCN) at 12 mol % LiBF4 and wherein the other electrochemical cell includes a catholyte including EC:EMC+1 M LiPF6+2 wt % monofluoroethylene carbonate (FEC). In the figure, circles refer to succinonitrile+12 mol % LiBF4, and triangles refer to EC:EMC+1 M LiPF6+2 wt % FEC.
FIG. 4 shows a plot of active mass-specific discharge capacity (mAh/g) as a function of cycle index for devices made according to Example 2 with two different catholytes.
FIG. 5 shows a plot of the median charge and discharge ASRdc (Ω-cm2) for two electrochemical cells, both stored at 4.6 V, and wherein one electrochemical cell includes a catholyte including succinonitrile at 12 mol % LiBF4 and wherein the other electrochemical cell includes a catholyte including EC:EMC+1 M LiPF6+2 wt % FEC. In the figure, circles refer to succinonitrile+12 mol % LiBF4, and triangles refer to EC:EMC at 3.7 w/w+1 M LiPF6+2 wt % FEC.
FIG. 6 shows a plot of mass percent of Gel Polymer Soaked in Electrolyte for two electrochemical cells, wherein one electrochemical cell includes a catholyte including adiponitrile and 1M LiTFSi and wherein the other electrochemical cell includes a catholyte including EC:EMC+1 M LiPF6+2 wt % FEC. In the figure, solid line is adiponitrile+1 M LiTFSi, and the doted line is EC:EMC+1 M LiPF6+2 wt % FEC.
FIG. 7 shows a plot of charge ASR growth wherein the cell is prepared with sulfolane and ethylene carbonate (3:7 v/v)+2M LiPF6 vs ethyl-methyl carbonate, ethylene carbonate (3:7 v/v)+1M LiPF6 for 10 cycles, C/3 pulses, from 2.7-4.2 V at 45° C. The cathode is NMC, and the separator is solid-state separator material. Solid line is EC:EMC 3:7 v/v+1 MLiPF6; dotted line is EC:Sulfolane 3:7 v/v+2 M LiPF6.
FIG. 8 shows a plot of discharge and charge ASR versus cycle life for 500 cycles for a cell.
DETAILED DESCRIPTION A. Definitions
As used herein, the term “about,” when qualifying a number, e.g., about 15% w/w, refers to the number qualified and optionally the numbers included in a range about that qualified number that includes ±10% of the number. For example, about 15% w/w includes 15% w/w as well as 13.5% w/w, 14% w/w, 14.5% w/w, 15.5% w/w, 16% w/w, or 16.5% w/w. For example, “about 75° C.,” includes 75° C. as well 68° C., 69° C., 70° C., 71° C., 72° C., 73° C., 74° C., 75° C., 76° C., 77° C., 78° C., 79° C., 80° C., 81° C., 82° C., or 83° C.
As used herein, the phrase “Li+ ion-conducting separator” refers to an electrolyte which conducts Li+ ions, is substantially insulating to electrons (e.g., the lithium ion conductivity is at least 103 times, and often 106 times, greater than the electron conductivity), and which acts as a physical barrier or spacer between the positive and negative electrodes in an electrochemical cell.
As used herein, the phrases “solid separator,” “solid electrolyte,” “solid-state separator,” and “solid-state electrolyte” refer to Li+ ion-conducting separators that are solids at room temperature and include at least 50 vol % ceramic material.
As used herein, “selected from the group consisting of” refers to a single member from the group, more than one member from the group, or a combination of members from the group. A member selected from the group consisting of A, B, and C includes, for example, A only, B only, or C only, as well as A and B, A and C, B and C, as well as A, B, and C.
As used herein, the phrase “electrochemical cell” refers to, for example, a “battery cell” and includes a positive electrode, a negative electrode, and an electrolyte therebetween which conducts ions (e.g., Li+) but electrically insulates the positive and negative electrodes. In some embodiments, a battery may include multiple positive electrodes and/or multiple negative electrodes enclosed in one container.
As used herein the phrase “electrochemical stack” refers to one or more units which each include at least a negative electrode (e.g., Li, LiC6), a positive electrode (e.g., Li-nickel-manganese-oxide or FeF3, optionally combined with a solid-state electrolyte or a gel electrolyte), and a solid electrolyte (e.g., an oxide electrolyte set forth herein, a lithium-stuffed garnet film, or a lithium-stuffed garnet pellet) between and in contact with the positive and negative electrodes. In some examples, between the solid electrolyte and the positive electrode, there is an additional layer comprising a compliant (e.g., gel electrolyte). An electrochemical stack may include one of these aforementioned units. An electrochemical stack may include several of these aforementioned units arranged in electrical communication (e.g., serial or parallel electrical connection). In some examples, when the electrochemical stack includes several units, the units are layered or laminated together in a column. In some examples, when the electrochemical stack includes several units, the units are layered or laminated together in an array. In some examples, when the electrochemical stack includes several units, the stacks are arranged such that one negative electrode is shared with two or more positive electrodes. Alternatively, in some examples, when the electrochemical stack includes several units, the stacks are arranged such that one positive electrode is shared with two or more negative electrodes. Unless specified otherwise, an electrochemical stack includes one positive electrode, one solid electrolyte, and one negative electrode, and optionally includes a gel electrolyte layer between the positive electrode and the solid electrolyte. In some examples, the gel electrolyte layer is also included in the positive electrode. In some examples, the gel electrolyte includes any electrolyte set forth herein, including a nitrile, dinitrile, organic sulfur-including solvent, or combination thereof set forth herein.
As used herein, the term “electrolyte” refers to a material that allows ions, e.g., Li+, to migrate or conduct therethrough but which does not allow electrons to conduct therethrough. Electrolytes are useful for electrically isolating the cathode and anodes of a secondary battery while allowing ions, e.g., Li+, to transmit through the electrolyte. Solid electrolytes, in particular, rely on ion hopping through rigid structures. Solid electrolytes may be also referred to as fast ion conductors or super-ionic conductors. Solid electrolytes may be also used for electrically insulating the positive and negative electrodes of a cell while allowing for the conduction of ions, e.g., Li+, through the electrolyte. In this case, a solid electrolyte layer may be also referred to as a solid electrolyte separator or solid-state electrolyte separator.
As used herein, the phrases “gel electrolyte” unless specified otherwise, refers to a suitable Li+ ion conducting gel or liquid-based electrolyte, for example, those set forth in U.S. Pat. No. 5,296,318, entitled RECHARGEABLE LITHIUM INTERCALATION BATTERY WITH HYBRID POLYMERIC ELECTROLYTE. A gel electrolyte has a lithium ion conductivity of greater than 10−5 S/cm at room temperature, a lithium transference number between 0.05-0.95, and a storage modulus greater than the loss modulus at some temperature. A gel electrolyte may comprise a polymer matrix, a solvent that gels the polymer, and a lithium containing salt that is at least partly dissociated into Li+ ions and anions. Alternately, a gel electrolyte may comprise a porous polymer matrix, a solvent that fills the pores, and a lithium containing salt that is at least partly dissociated into Li+ ions and anions where the pores have one length scale less than 10 μm.
As used herein, the term “laminating” refers to the process of sequentially depositing a layer of one precursor specie, e.g., a lithium precursor specie, onto a deposition substrate and then subsequently depositing an additional layer onto an already deposited layer using a second precursor specie, e.g., a transition metal precursor specie. This laminating process can be repeated to build up several layers of deposited vapor phases. As used herein, the term “laminating” also refers to the process whereby a layer comprising an electrode, e.g., positive electrode or cathode active material comprising layer, is contacted to a layer comprising another material, e.g., garnet electrolyte. The term “laminating” also refers to the process whereby at least two layers comprising a solid electrolyte material are contacted together. The laminating process may include a reaction or use of a binder which adheres of physically maintains the contact between the layers which are laminated. The process of laminating one layer to another layer results in one layer being laminated to the other layer.
As used herein, the phrase “directly contacts” refers to the juxtaposition of two materials such that the two materials contact each other sufficiently to conduct either an ion or electron current. As used herein, direct contact refers to two materials in contact with each other and which do not have any materials positioned between the two materials which are in direct contact.
As used herein, the terms “cathode” and “anode” refer to the electrodes of a battery. The cathode and anode are often referred to in the relevant field as the positive electrode and negative electrode, respectively. During a charge cycle in a Li-secondary battery, Li ions leave the cathode and move through an electrolyte, to the anode. During a charge cycle, electrons leave the cathode and move through an external circuit to the anode. During a discharge cycle in a Li-secondary battery, Li ions migrate towards the cathode through an electrolyte and from the anode. During a discharge cycle, electrons leave the anode and move through an external circuit to the cathode.
As used herein, the phrase “positive electrode” refers to the electrode in a secondary battery towards which positive ions, e.g., Li+, conduct, flow or move during discharge of the battery. As used herein, the phrase “negative electrode” refers to the electrode in a secondary battery from where positive ions, e.g., Li+, flow or move during discharge of the battery. In a battery comprised of a Li-metal electrode and a conversion chemistry, intercalation chemistry, or combination conversion/intercalation chemistry-including electrode (i.e., cathode active material; e.g., NiFx, NCA, LiNixMnyCozO2 [NMC] or LiNixAlyCozO2 [NCA], wherein x+y+z=1), the electrode having the conversion chemistry, intercalation chemistry, or combination conversion/intercalation chemistry material is referred to as the positive electrode. In some common usages, cathode is used in place of positive electrode, and anode is used in place of negative electrode. When a Li-secondary battery is charged, Li ions move from the positive electrode (e.g., NiFx, NMC, NCA) towards the negative electrode (e.g., Li-metal). When a Li-secondary battery is discharged, Li ions move towards the positive electrode and from the negative electrode.
As used herein, the term “catholyte” refers to a Li ion conductor that is intimately mixed with, or that surrounds and contacts, or that contacts the positive electrode active materials and provides an ionic pathway for Li+ to and from the active materials. Catholytes suitable with the embodiments described herein include, but are not limited to, catholytes having the acronyms name LPS, LXPS, LXPSO, where X is Si, Ge, Sn, As, Al, LATS, or also Li-stuffed garnets, or combinations thereof, and the like. Catholytes may also be liquid, gel, semi-liquid, semi-solid, polymer, and/or solid polymer ion conductors known in the art. In some examples, the catholyte includes a gel set forth herein. In some examples, the gel electrolyte includes any electrolyte set forth herein, including a nitrile, dinitrile, organic sulfur-including solvent, or combination thereof set forth herein.
In some examples, the electrolytes herein may include, or be layered with, or be laminated to, or contact a sulfide electrolyte. As used here, the phrase “sulfide electrolyte,” includes, but is not limited to, electrolytes referred to herein as LSS, LTS, LXPS, or LXPSO, where X is Si, Ge, Sn, As, Al, LATS. In these acronyms (LSS, LTS, LXPS, or LXPSO), S refers to the element S, Si, or combinations thereof, and T refers to the element Sn. “Sulfide electrolyte” may also include LiaPbScXd, LiaBbScXd, LiaSnbScXd or LiaSibScXd where X═F, Cl, Br, I, and 10%≤a≤50%, 10%≤b≤44%, 24%≤c≤70%, 0≤d≤18% and may further include oxygen in small amounts. For example, oxygen may be present as a dopant or in an amount less than 10 percent by weight. For example, oxygen may be present as a dopant or in an amount less than 5 percent by weight.
As used herein, the phrase “sulfide based electrolytes” refers to electrolytes that include inorganic materials containing S which conduct ions (e.g., Li+) and which are suitable for electrically insulating the positive and negative electrodes of an electrochemical cell (e.g., secondary battery). Exemplary sulfide based electrolytes include, but are not limited to, those electrolytes set forth in International Patent Application PCT Patent Application No. PCT/US14/38283, SOLID STATE CATHOLYTE OR ELECTROLYTE FOR BATTERY USING LiAMPBSC (M=SI, GE, AND/OR SN), filed May 15, 2014, and published as WO 2014/186634, on Nov. 20, 2014, which is incorporated by reference herein in its entirety; also, U.S. Pat. No. 8,697,292 to Kanno, et al, the contents of which are incorporated by reference in their entirety.
As used here, the phrase “sulfide electrolyte” includes, but are not limited to, LSS, LTS, LXPS, LXPSO, where X is Si, Ge, Sn, As, Al, LATS, also Li-stuffed garnets, or combinations thereof, and the like, S is S, Si, or combinations thereof, T is Sn.
As used herein, “SLOPS” includes, unless otherwise specified, a 60:40 molar ratio of Li2S:SiS2 with 0.1-10 mol. % Li3PO4. In some examples, “SLOPS” includes Li10Si4S13 (50:50 Li2S:SiS2) with 0.1-10 mol. % Li3PO4. In some examples, “SLOPS” includes Li26Si7S27 (65:35 Li2S:SiS2) with 0.1-10 mol. % Li3PO4. In some examples, “SLOPS” includes Li4SiS4 (67:33 Li2S:SiS2) with 0.1-5 mol. % Li3PO4. In some examples, “SLOPS” includes Li14Si3S13 (70:30 Li2S:SiS2) with 0.1-5 mol. % Li3PO4. In some examples, “SLOPS” is characterized by the formula (1−x)(60:40 Li2S:SiS2)*(x)(Li3PO4), wherein x is from 0.01 to 0.99. As used herein, “LBS-POX” refers to an electrolyte composition of Li2S:B2S3:Li3PO4:LiX where X is a halogen (X═F, Cl, Br, I). The composition can include Li3BS3 or Li5B7S13 doped with 0-30% lithium halide such as LiI and/or 0-10% Li3PO4.
As used here, “LBS” refers to an electrolyte material characterized by the formula LiaBbSc and may include oxygen and/or a lithium halide (LiF, LiCl, LiBr, LiI) at 0-40 mol %.
As used here, “LPSO” refers to an electrolyte material characterized by the formula LixPySzOw where 0.33≤x≤0.67, 0.07≤y≤0.2, 0.4≤z≤0.55, 0≤w≤0.15. Also, LPSO refers to LPS, as defined above, that includes an oxygen content of from 0.01 to 10 atomic %. In some examples, the oxygen content is 1 atomic %. In other examples, the oxygen content is 2 atomic %. In some other examples, the oxygen content is 3 atomic %. In some examples, the oxygen content is 4 atomic %. In other examples, the oxygen content is 5 atomic %. In some other examples, the oxygen content is 6 atomic %. In some examples, the oxygen content is 7 atomic %. In other examples, the oxygen content is 8 atomic %. In some other examples, the oxygen content is 9 atomic %. In some examples, the oxygen content is 10 atomic %.
As used herein, the term “LBHI” or “LiBHI” refers to a lithium conducting electrolyte comprising Li, B, H, and I. More generally, it is understood to include aLiBH4+bLiX where X═Cl, Br, and/or I and where a:b=7:1, 6:1, 5:1, 4:1, 3:1, 2:1, or within the range a/b=2-4. LBHI may further include nitrogen in the form of aLiBH4+bLiX+cLiNH2 where (a+c)/b=2-4 and c/a=0-10.
As used herein, the term “LPSI” refers to a lithium conducting electrolyte comprising Li, P, S, and I. More generally, it is understood to include aLi2S+bP2Sy+cLiX where X═Cl, Br, and/or I and where y=3-5 and where a/b=2.5-4.5 and where (a+b)/c=0.5-15.
As used herein, the term “LIRAP” refers to a lithium rich antiperovskite and is used synonymously with “LOC” or “Li3OCl”. The composition of LIRAP is aLi2O+bLiX+cLiOH+dAl2O3 where X═Cl, Br, and/or I, a/b=0.7-9, c/a=0.01-1, d/a=0.001-0.1.
As used herein, “LSS” refers to lithium silicon sulfide which can be described as Li2S—SiS2, Li—SiS2, Li—S—Si, and/or a catholyte consisting essentially of Li, S, and Si. LSS refers to an electrolyte material characterized by the formula LixSiySz where 0.33≤x≤0.5, 0.1≤y≤0.2, 0.4≤z≤0.55, and it may include up to 10 atomic % oxygen. LSS also refers to an electrolyte material comprising Li, Si, and S. In some examples, LSS is a mixture of Li2S and SiS2. In some examples, the ratio of Li2S:SiS2 is 90:10, 85:15, 80:20, 75:25, 70:30, 2:1, 65:35, 60:40, 55:45, or 50:50 molar ratio. LSS may be doped with compounds such as LixPOy, LixBOy, Li4SiO4, Li3MO4, Li3MO3, PSx, and/or lithium halides such as, but not limited to, LiI, LiCl, LiF, or LiBr, wherein 0<x≤5 and 0≤y≤5.
As used herein, “LTS” refers to a lithium tin sulfide compound which can be described as Li2S—SnS2, Li2S—SnS, Li—S—Sn, and/or a catholyte consisting essentially of Li, S, and Sn. The composition may be LixSnySz where 0.25≤x≤0.65, 0.05≤y≤0.2, and 0.25≤z≤0.65. In some examples, LTS is a mixture of Li2S and SnS2 in the ratio of 80:20, 75:25, 70:30, 2:1, or 1:1 molar ratio. LTS may include up to 10 atomic % oxygen. LTS may be doped with Bi, Sb, As, P, B, Al, Ge, Ga, and/or In. As used herein, “LATS” refers to LTS, as used above, and further comprising Arsenic (As).
As used herein, “LXPS” refers to a material characterized by the formula LiaMPbSc, where M is Si, Ge, Sn, and/or Al, and where 2≤a≤8, 0.5≤b≤2.5, 4≤c≤12. “LSPS” refers to an electrolyte material characterized by the formula LaSiPbSc, where 2≤a≤8, 0.5≤b≤2.5, 4≤c≤12. LSPS refers to an electrolyte material characterized by the formula LaSiPbSc, wherein, where 2≤a≤8, 0.5≤b≤2.5, 4≤c≤12, d≤3. Exemplary LXPS materials are found, for example, in International Patent Application No. PCT/US14/38283, SOLID STATE CATHOLYTE OR ELECTROLYTE FOR BATTERY USING LiAMPBSC (M=SI, GE, AND/OR SN), filed May 15, 2014, and published as WO 2014/186634, on Nov. 20, 2014, which is incorporated by reference herein in its entirety. Exemplary LXPS materials are found, for example, in U.S. patent application Ser. No. 14/618,979, filed Feb. 10, 2015, and published as Patent Application Publication No. 2015/0171465, on Jun. 18, 2015, which is incorporated by reference herein in its entirety. When M is Sn and Si—both are present—the LXPS material is referred to as LSTPS. As used herein, “LSTPSO” refers to LSTPS that is doped with, or has, O present. In some examples, “LSTPSO” is a LSTPS material with an oxygen content between 0.01 and 10 atomic %. “LSPS” refers to an electrolyte material having Li, Si, P, and S chemical constituents. As used herein “LSTPS” refers to an electrolyte material having Li, Si, P, Sn, and S chemical constituents. As used herein, “LSPSO” refers to LSPS that is doped with, or has, O present. In some examples, “LSPSO” is a LSPS material with an oxygen content between 0.01 and 10 atomic %. As used herein, “LATP,” refers to an electrolyte material having Li, As, Sn, and P chemical constituents. As used herein “LAGP” refers to an electrolyte material having Li, As, Ge, and P chemical constituents. As used herein, “LXPSO” refers to a catholyte material characterized by the formula LiaMPbScOd, where M is Si, Ge, Sn, and/or Al, and where 2≤a≤8, 0.5≤b≤2.5, 4≤c≤12, d<3. LXPSO refers to LXPS, as defined above, and having oxygen doping at from 0.1 to about 10 atomic %. LPSO refers to LPS, as defined above, and having oxygen doping at from 0.1 to about 10 atomic %.
As used herein, “LPS” refers to an electrolyte having Li, P, and S chemical constituents. As used herein, “LPSO” refers to LPS that is doped with or has O present. In some examples, “LPSO” is a LPS material with an oxygen content between 0.01 and 10 atomic %. LPS refers to an electrolyte material that can be characterized by the formula LixPySz where 0.33≤x≤0.67, 0.07≤y≤0.2 and 0.4≤z≤0.55. LPS also refers to an electrolyte characterized by a product formed from a mixture of Li2S:P2S5 wherein the molar ratio is 10:1, 9:1, 8:1, 7:1, 6:1 5:1, 4:1, 3:1, 7:3, 2:1, or 1:1. LPS also refers to an electrolyte characterized by a product formed from a mixture of Li2S:P2S5 wherein the reactant or precursor amount of Li2S is 95 atomic % and P2S5 is 5 atomic %. LPS also refers to an electrolyte characterized by a product formed from a mixture of Li2S:P2S5 wherein the reactant or precursor amount of Li2S is 90 atomic % and P2S5 is 10 atomic %. LPS also refers to an electrolyte characterized by a product formed from a mixture of Li2S:P2S5 wherein the reactant or precursor amount of Li2S is 85 atomic % and P2S5 is 15 atomic %. LPS also refers to an electrolyte characterized by a product formed from a mixture of Li2S:P2S5 wherein the reactant or precursor amount of Li2S is 80 atomic % and P2S5 is 20 atomic %. LPS also refers to an electrolyte characterized by a product formed from a mixture of Li2S:P2S5 wherein the reactant or precursor amount of Li2S is 75 atomic % and P2S5 is 25 atomic %. LPS also refers to an electrolyte characterized by a product formed from a mixture of Li2S:P2S5 wherein the reactant or precursor amount of Li2S is 70 atomic % and P2S5 is 30 atomic %. LPS also refers to an electrolyte characterized by a product formed from a mixture of Li2S:P2S5 wherein the reactant or precursor amount of Li2S is 65 atomic % and P2S5 is 35 atomic %. LPS also refers to an electrolyte characterized by a product formed from a mixture of Li2S:P2S5 wherein the reactant or precursor amount of Li2S is 60 atomic % and P2S5 is 40 atomic %.
As used herein, the term “rational number” refers to any number which can be expressed as the quotient or fraction (e.g., p/q) of two integers (e.g., p and q), with the denominator (e.g., q) not equal to zero. Example rational numbers include, but are not limited to, 1, 1.1, 1.52, 2, 2.5, 3, 3.12, and 7.
As used herein, the phrase “lithium stuffed garnet” refers to oxides that are characterized by a crystal structure related to a garnet crystal structure. U.S. Patent Application Publication No. U.S. 2015/0099190, which published Apr. 9, 2015 and was filed Oct. 7, 2014 as Ser. No. 14/509,029, is incorporated by reference herein in its entirety. This application describes Li-stuffed garnet solid-state electrolytes used in solid-state lithium rechargeable batteries. These Li-stuffed garnets generally having a composition according to LiALaBM′CM″DZrEOF, LiALaBM′CM″DTaEOF, or LiALaBM′CM″DNbEOF, wherein 4<A<8.5, 1.5<B<4, 0≤C≤2, 0≤D≤2; 0≤E<2.5, 10<F<13, and M′ and M″ are each, independently in each instance selected from Ga, Al, Mo, W, Nb, Sb, Ca, Ba, Sr, Ce, Hf, Rb, and Ta, or LiaLabZrcAldMe″eOf, wherein 5<a<8.5; 2<b<4; 0<c≤2.5; 0≤d<2; 0≤e<2, and 10<f<13 and Me″ is a metal selected from Ga, Nb, Ta, V, W, Mo, and Sb and as otherwise described in U.S. Patent Application Publication No. U.S. 2015/0099190. As used herein, lithium-stuffed garnets, and garnets, generally, include, but are not limited to, Li7.0La3(Zrt1+Nbt2+Tat3)O12+0.35Al2O3; wherein (t1+t2+t3=2) so that the La:(Zr/Nb/Ta) ratio is 3:2. Also, garnets used herein include, but are not limited to, LixLa3Zr2OF+yAl2O3, wherein x ranges from 5.5 to 9; and y ranges from 0.05 to 1. In these examples, subscripts x, y, and F are selected so that the garnet is charge neutral. In some examples x is 7 and y is 1.0. In some examples, x is 5 and y is 1.0. In some examples, x is 6 and y is 1.0. In some examples, x is 8 and y is 1.0. In some examples, x is 9 and y is 1.0. In some examples x is 7 and y is 0.35. In some examples, x is 5 and y is 0.35. In some examples, x is 6 and y is 0.35. In some examples, x is 8 and y is 0.35. In some examples, x is 9 and y is 0.35. In some examples x is 7 and y is 0.7. In some examples, x is 5 and y is 0.7. In some examples, x is 6 and y is 0.7. In some examples, x is 8 and y is 0.7. In some examples, x is 9 and y is 0.7. In some examples x is 7 and y is 0.75. In some examples, x is 5 and y is 0.75. In some examples, x is 6 and y is 0.75. In some examples, x is 8 and y is 0.75. In some examples, x is 9 and y is 0.75. In some examples x is 7 and y is 0.8. In some examples, x is 5 and y is 0.8. In some examples, x is 6 and y is 0.8. In some examples, x is 8 and y is 0.8. In some examples, x is 9 and y is 0.8. In some examples x is 7 and y is 0.5. In some examples, x is 5 and y is 0.5. In some examples, x is 6 and y is 0.5. In some examples, x is 8 and y is 0.5. In some examples, x is 9 and y is 0.5. In some examples x is 7 and y is 0.4. In some examples, x is 5 and y is 0.4. In some examples, x is 6 and y is 0.4. In some examples, x is 8 and y is 0.4. In some examples, x is 9 and y is 0.4. In some examples x is 7 and y is 0.3. In some examples, x is 5 and y is 0.3. In some examples, x is 6 and y is 0.3. In some examples, x is 8 and y is 0.3. In some examples, x is 9 and y is 0.3. In some examples x is 7 and y is 0.22. In some examples, x is 5 and y is 0.22. In some examples, x is 6 and y is 0.22. In some examples, x is 8 and y is 0.22. In some examples, x is 9 and y is 0.22. Also, garnets as used herein include, but are not limited to, LixLa3Zr2O12+yAl2O3. In one embodiment, the Li-stuffed garnet herein has a composition of Li7Li3Zr2O12. In another embodiment, the Li-stuffed garnet herein has a composition of Li7Li3Zr2O12.Al2O3. In yet another embodiment, the Li-stuffed garnet herein has a composition of Li7Li3Zr2O120.22Al2O3. In yet another embodiment, the Li-stuffed garnet herein has a composition of Li7Li3Zr2O12.0.35Al2O3. In certain other embodiments, the Li-stuffed garnet herein has a composition of Li7Li3Zr2O12.0.5Al2O3. In another embodiment, the Li-stuffed garnet herein has a composition of Li7Li3Zr2O12.0.75Al2O3.
As used herein, garnet does not include YAG-garnets (i.e., yttrium aluminum garnets, or, e.g., Y3Al5O12). As used herein, garnet does not include silicate-based garnets such as pyrope, almandine, spessartine, grossular, hessonite, or cinnamon-stone, tsavorite, uvarovite and andradite and the solid solutions pyrope-almandine-spessarite and uvarovite-grossular-andradite. Garnets herein do not include nesosilicates having the general formula X3Y2(SiO4)3 wherein X is Ca, Mg, Fe, and, or, Mn; and Y is Al, Fe, and, or, Cr.
As used herein, the phrase “inorganic solid-state electrolyte” is used interchangeably with the phrase “solid separator” refers to a material which does not include carbon and which conducts atomic ions (e.g., Li+) but does not conduct electrons. An inorganic solid-state electrolyte is a solid material suitable for electrically isolating the positive and negative electrodes of a lithium secondary battery while also providing a conduction pathway for lithium ions. Example inorganic solid-state electrolytes include oxide electrolytes and sulfide electrolytes, which are further defined below. Non-limiting example sulfide electrolytes are found, for example, in U.S. Pat. No. 9,172,114, which issued Oct. 27, 2015, and also in U.S. Provisional Patent Application No. 62/321,428, filed Apr. 12, 2016. Non-limiting example oxide electrolytes are found, for example, in US Patent Application Publication No. 2015-0200420 A1, which published Jul. 16, 2015. In some examples, the inorganic solid-state electrolyte also includes a polymer.
As used herein, examples of the materials in International Patent Application PCT Patent Application Nos. PCT/US2014/059575 and PCT/US2014/059578, GARNET MATERIALS FOR LI SECONDARY BATTERIES AND METHODS OF MAKING AND USING GARNET MATERIALS, filed Oct. 7, 2014, which is incorporated by reference herein in its entirety, are suitable for use as the inorganic solid-state electrolytes described herein, also as the oxide based electrolytes, described herein, and also as the garnet electrolytes, described herein.
As used herein the phrase “casting a film” refers to the process of delivering or transferring a liquid or a slurry into a mold, or onto a substrate, such that the liquid or the slurry forms, or is formed into, a film. Casting may be done via doctor blade, Meyer rod, comma coater, gravure coater, microgravure, reverse comma coater, slot dye, slip and/or tape casting, and other methods known to those skilled in the art.
As used herein, the phrase “slot casting” refers to a deposition process whereby a substrate is coated, or deposited, with a solution, liquid, slurry, or the like by flowing the solution, liquid, slurry, or the like, through a slot or mold of fixed dimensions that is placed adjacent to, in contact with, or onto the substrate onto which the deposition or coating occurs. In some examples, slot casting includes a slot opening of about 1 μm to 100 μm in slot opening width.
As used herein, the phrase “dip casting” or “dip coating” refers to a deposition process whereby substrate is coated, or deposited, with a solution, liquid, slurry, or the like, by moving the substrate into and out of the solution, liquid, slurry, or the like, often in a vertical fashion.
As used herein the term “making” refers to the process or method of forming or causing to form the object that is made. For example, making an energy storage electrode includes the process, process steps, or method of causing the electrode of an energy storage device to be formed. The end result of the steps constituting the making of the energy storage electrode is the production of a material that is functional as an electrode.
As used herein, the phrase “providing” refers to the provision of, generation or, presentation of, or delivery of that which is provided.
As used herein, the phrase “garnet-type electrolyte” refers to an electrolyte that includes a garnet or lithium stuffed garnet material described herein as the ionic conductor.
As used herein, the phrase “antiperovskite” refers to an electrolyte characterized by the antiperovskite crystal structure. Exemplary antiperovskites are found, for example, in U.S. patent application Ser. No. 13/777,602, filed Feb. 26, 2013. Antiperovskites include but are not limited to Li3OBr or Li3OCl.
As used herein, the phrase “subscripts and molar coefficients in the empirical formulas are based on the quantities of raw materials initially batched to make the described examples” means the subscripts, (e.g., 7, 3, 2, 12 in Li7La3Zr2O12 and the coefficient 0.35 in 0.35Al2O3) refer to the respective elemental ratios in the chemical precursors (e.g., LiOH, La2O3, ZrO2, Al2O3) used to prepare a given material, (e.g., Li7La3Zr2O12.0.35Al2O3). As used here, the phrase “characterized by the formula” refers to a molar ratio of constituent atoms either as batched during the process for making that characterized material or as empirically determined.
As used herein, the term “solvent” refers to a liquid that is suitable for dissolving or solvating a component or material described herein. For example, a solvent includes a liquid, e.g., propylene carbonate, which is suitable for dissolving a component, e.g., the salt, used in the electrolyte.
As used herein, the phrase “removing a solvent” refers to the process whereby a solvent is extracted or separated from the components or materials set forth herein. Removing a solvent includes, but is not limited to, evaporating a solvent. Removing a solvent includes, but is not limited to, using a vacuum or a reduced pressure to drive off a solvent from a mixture, e.g., an unsintered thin film. In some examples, a thin film that includes a binder and a solvent is heated or also optionally placed in a vacuum or reduced atmosphere environment in order to evaporate the solvent to leave the binder, which was solvated, in the thin film after the solvent is removed.
As used herein, the phrase “nitrile” or “nitrile solvent” refers to a hydrocarbon substituted by a cyano group, or a solvent which includes a cyano (i.e., —C≡N) substituent bonded to the solvent. Nitrile solvents may include dinitrile solvents.
As used herein, the phrase “dinitrile” or “dinitrile solvent” refers to a linear hydrocarbon chain where both ends of the chain are terminated with a cyano (i.e., —C≡N) group. Example dinitrile solvents are characterized by Formula (I):
Figure US11342630-20220524-C00001

wherein:
R1, R2, R3, and R4 are, independently in each instance, selected from —CN, —NO2, —CO2, —SO4, —H, —SO3, —SO2, —CH2—SO3, —CHF—SO3, —CF2—SO3, —F, —Cl, —Br, and —I; and wherein subscript m is an integer from 1 to 1000.
Some exemplary nitrile and dinitrile solvents include, but are not limited to, acetonitrile, succinonitrile, glutaronitrile, malononitrile, hexanedinitrile (adiponitrile), sebaconitrile, suberonitrile, pimelonitrile, dodecanedinitrile, phthalonitrile, cis/trans-1,2-dicyanocyclohexane, and combinations thereof.
As used herein, the phrase “organic sulfur-including solvent” refers to a solvent selected from ethyl methyl sulfone, dimethyl sulfone, sulfolane, allyl methyl sulfone, butadiene sulfone, butyl sulfone, methyl methanesulfonate, and dimethyl sulfite.
As used herein, the phrase “impermeable to the catholyte” refers to a material that allows a low flux of catholyte to permeate, for example less than 1 g/cm2/year, through the material, e.g., a solid separator, which is impermeable to the catholyte or its constituent components.
As used herein, the phrase “bonding layer” refers to an ionically conductive layer between two other layers, e.g., between the cathode and the solid separator. Exemplary bonding layers include the gel electrolytes, and related separator bonding agents, set forth in U.S. Provisional Patent Application No. 62/336,474, filed May 13, 2016, the entire contents of which are herein incorporated by reference in its entirety for all purposes.
As used herein, the term “HOMO” or “Highest Occupied Molecular Orbital” refers to the energy of the electron occupying the highest occupied molecular orbital, as referenced to the vacuum energy. As used herein, the term “LUMO” refers to “Lowest Unoccupied Molecular Orbital.” HOMO and LUMO energy levels are calculated by DFT calculations referenced to the vacuum level. Unless otherwise specified, the DFT calculations use a B3LYP functional for exchange and correlation and a 6-311++g** basis set.
As used herein, the phrase “lithium transference” refers to the proportion of current carried by lithium ions relative to the total current. Lithium transference is a number between 0 and 1, inclusive and may be measured by the Bruce-Vincent method.
As used herein, the phrase “stability window” refers to the voltage range within which a material exhibits no reaction which materially or significantly degrades the material's function in an electrochemical cell. It may be measured in an electrochemical cell by measuring cell resistance and Coulombic efficiency during charge/discharge cycling. For voltages within the stability window (i.e. the working electrode vs reference electrode within the stability window), the increase of cell resistance is low. For example, this resistance increase may be less than 1% per 100 cycles.
As used herein, the term “LiBOB” refers to lithium bis(oxalato)borate.
As used herein, the term “LiBETI” refers to lithium bis(perfluoroethanesulfonyl)imide.
As used herein, the term “LIFSI” refers to lithium bis(fluorosulfonyl)imide.
As used herein, the term “LiTFSI” refer to lithium bis-trifluoromethanesulfonimide.
As used herein, voltage is set forth with respect to lithium (i.e., V vs. Li) metal unless stated otherwise.
As used herein, the term “LiBHI” refers to a combination of LiBH4 and LiX, wherein X is Br, Cl, I, or a combination thereof.
As used herein, the term “LiBNHI” refers to a combination of LiBH4, LiNH2, and LiX, wherein X is Br, Cl, I, or combinations thereof.
As used herein, the term “LiBHCl” refers to a combination of LiBH4 and LiCl.
As used herein, the term “LiBNHCl” refers to a combination of LiBH4, LiNH2, and LiCl.
As used herein, the term “LiBHBr” refers to a combination of LiBH4 and LiBr.
As used herein, the term “LiBNHBr” refers to a combination of LiBH4, LiNH2, and LiBr.
As used herein, viscosity is measured using a Brookfield viscometer DV2T.
As used herein, the term “monolith” refers to a shaped, fabricated article with a homogenous microstructure with no structural distinctions observed optically, which has a form factor top surface area between 10 cm2 and 500 cm2.
As used herein, the term “vapor pressure” refers to the equilibrium pressure of a gas above its liquid at the same temperature in a closed system. Measurement procedures often consist of purifying the test substance, isolating it in a container, evacuating any foreign gas, then measuring the equilibrium pressure of the gaseous phase of the substance in the container at different temperatures. Better accuracy is achieved when care is taken to ensure that the entire substance and its vapor are at the prescribed temperature. This is often done, as with the use of an isoteniscope, by submerging the containment area in a liquid bath.
As used herein, the term “lithium salt” refers to a lithium-containing compound that is a solid at room temperature that at least partially dissociates when immersed in a solvent such as EMC. Lithium salts may include but are not limited to LiPF6, LiBOB, LiTFSi, LiFSI, LiAsF6, LiClO4, LiI, LiBETI, LiBF4.As used herein, the term “carbonate solvent” refers to a class of solvents containing a carbonate group C(═O)(O—)2. Carbonate solvents include but are not limited to ethylene carbonate, dimethyl carbonate, propylene carbonate, diethyl carbonate, ethyl methyl carbonate, dimethyl ethylene carbonate, isobutylene carbonate, nitroethyl carbonate, Monofluoroethylene carbonate, fluoromethyl ethylene carbonate, 1,2-butylene carbonate, methyl propyl carbonate, isopropyl methyl carbonate, etc.
As used herein, the term “a high voltage-stable catholyte” refers to a catholyte which does not react at high voltage (4.2 V or higher versus Li metal) in a way that materially or significantly degrades the ionic conductivity of the catholyte when held at high voltage at room temperature for one week. Herein, a material or significant degradation in ionic conductivity is a reduction in ionic conductivity by an order of magnitude or more. For example, if the catholyte has an ionic conductivity of 10E-3 S/cm, and when charged to 4.2V or higher the catholyte has an ionic conductivity of 10E-4 S/cm, then the catholyte is not stable at 4.2V or higher since its ionic conductivity materially and significantly degraded at that voltage.” As used herein, the term “high voltage” means at least 4.2V versus lithium metal. High voltage may also refer to higher voltage, e.g., 4.3, 4.4, 4.5, 4.6, 4.7, 4.8. 4.9, 5.0 V or higher.
As used herein, the term “chemically compatible” means that two or more materials or chemicals are chemically compatible with each other if the materials can be physically exposed to each other and the materials do not react in a way which materially or significantly degrades the electrochemical performance. Herein, electrochemical performance refers to either ionic conductivity or area-specific resistance (ASR). A material or significant degradation in ionic conductivity is a degradation by an order of magnitude or more. A material or significant degradation in ASR is a degradation by a factor of 2 or more when held at room temperature for one week.
As used herein, ASR is measured by electrochemical cycling using Arbin or Biologic unless otherwise specified to the contrary.
As used herein, ionic conductivity is measured by electrical impedance spectroscopy methods known in the art.
B. General
Set forth herein are battery architectures for batteries which include a solid-state separator which physically isolates the cathode from the anode. These architectures allow, for the first time in a rechargeable lithium battery, the use of electrolytes in the cathode, i.e., catholytes, that have no stability requirement against lithium metal or graphite, e.g., high-voltage (greater than 4.3V) stable dinitrile electrolytes. These electrolytes have advantageous properties including safety, lifetime, cyclability, voltage stability, and rate performance. In some examples, set forth herein are devices that include a high voltage, nitrile, or dinitrile or organic sulfur-including cathode-electrolyte (i.e., catholyte) which is stable at high oxidation potentials within the cathode side of an electrochemical device having a solid-state separator. The new battery architectures presented for the first time herein are not possible in a conventional Li-ion battery. Conventional battery architectures use catholytes which penetrate the anode space and therefore must be stable and/or passivating at the anode voltage and also chemically compatible with the anode materials. It is only by using a solid-state separator that the nitrile and high voltage-stable catholytes herein can be used practically in electrochemical devices as catholytes or electrolytes within the cathode space. In some examples, set forth herein are nitrile catholytes which are stable at high voltages with respect to lithium but which are not stable at low voltages with respect to lithium. In some examples, set forth herein are organic sulfur-including catholytes which are stable at high voltages with respect to lithium but which are not stable at low voltages (e.g. less than 1.5V or less than 1V) with respect to lithium, meaning that they significantly degrade in impedance or conductivity at room temperature for one week.
As shown in FIG. 1, in one example, an electrochemical cell (100) includes a positive electrode 101 of 5-200 μm thickness. This electrode 101 includes active materials 102 surrounded by a cathode-electrolyte 103. Active materials 102 may be present in 20-80 vol %, and the catholyte may be present in 5-60 vol %. The electrode 101 is layered to a solid separator 104 (e.g., a lithium-stuffed garnet electrolyte monolith or thin film). The solid separator 104 is layered to a lithium-metal negative electrode 105. The solid separator 104 may be 100 nm-100 μm thick, and the lithium metal negative electrode 105 may be 1 μm-50 μm thick. The solid separator 104 is impermeable to the catholyte-electrolyte 103.
In certain examples, the positive electrode is from 30 μm to 300 μm thick. In some examples, the positive electrode is from 40 μm to 200 μm thick. In some of these examples, the positive electrode is about 30 μm thick. In some of these examples, the positive electrode is about 40 μm thick. In some of these examples, the positive electrode is about 50 μm thick. In some of these examples, the positive electrode is about 60 μm thick. In some of these examples, the positive electrode is about 70 μm thick. In some of these examples, the positive electrode is about 80 μm thick. In some of these examples, the positive electrode is about 90 μm thick. In some of these examples, the positive electrode is about 100 μm thick. In some of these examples, the positive electrode is about 110 μm thick. In some of these examples, the positive electrode is about 120 μm thick. In some of these examples, the positive electrode is about 130 μm thick. In some of these examples, the positive electrode is about 140 μm thick. In some of these examples, the positive electrode is about 150 μm thick. In some of these examples, the positive electrode is about 160 μm thick. In some of these examples, the positive electrode is about 170 μm thick. In some of these examples, the positive electrode is about 180 μm thick. In some of these examples, the positive electrode is about 190 μm thick. In some of these examples, the positive electrode is about 200 μm thick. In some of these examples, the positive electrode is about 210 μm thick. In some of these examples, the positive electrode is about 220 μm thick. In some of these examples, the positive electrode is about 230 μm thick. In some of these examples, the positive electrode is about 240 μm thick. In some of these examples, the positive electrode is about 250 μm thick. In some of these examples, the positive electrode is about 260 μm thick. In some of these examples, the positive electrode is about 270 μm thick. In some of these examples, the positive electrode is about 280 μm thick. In some of these examples, the positive electrode is about 290 μm thick. In some of these examples, the positive electrode is about 300 μm thick.
The active material (e.g., a nickel manganese cobalt oxide, i.e., NMC, a nickel cobalt aluminum oxide, i.e., NCA, a lithium cobalt oxide, i.e., LCO, a lithium-rich nickel manganese oxide, i.e., LNMO, FeF3, CoF2, CuF2, CoF3, and related or functionally equivalent active materials) may be present in a volume fraction of 20-95%. In some examples, the volume fraction is 50-75 v %. The cathode electrolyte, or catholyte, may be present in a volume fraction of 10-50%. In some examples, the catholyte is present in a volume fraction of 20-40 volume %. The solid separator may be 0.5-100 μm thick. In some examples, the solid separator is 1-30 μm thick. The negative electrode may be 3-80 μm thick. In some examples, the negative electrode is 20-50 μm thick in the charged state.
In any of the above examples, the carbon content in the positive electrode is less than 5% w/w. In any of the above examples, the binder content in the positive electrode is less than 5% w/w.
C. Catholytes and Solid Separator Electrolytes
In some examples, set forth herein is a high voltage-stable catholyte which includes a solvent and a lithium salt. In some examples, the solvent is a nitrile solvent. In some examples, the solvent is a dinitrile solvent. In yet other examples, the solvent is a combination of a nitrile and dinitrile solvent. In yet other example the solvent is a combination of a dinitrile and another dinitrile. In yet other example, the solvent is an organic sulfur-including solvent. In yet another example, the solvent is a combination of an organic sulfur-including solvent and another aprotic solvent.
In some examples, set forth herein is a catholyte which includes a nitrile or dinitrile solvent and a lithium salt.
In some of these examples, the solvent in the catholyte is selected from the group consisting of from acetonitrile, butyronitrile, benzonitrile, glutaronitrile, hexanenitrile, fluoroacetonitrile, nitroacetonitrile, ethoxyacetonitrile, methoxyacetonitrile, pentanenitrile, propanenitrile, succinonitrile, adiponitrile, iso-butyronitrile, malononitrile and combinations thereof. In certain examples, the catholyte solvent is fluoromethyl ethylene carbonate, ethyl nitroacetate, N-Methylpyrrolidone, γ-butyrolactone, ethyl methyl sulfone, dimethyl sulfone, sulfolane, allyl methyl sulfone, butadiene sulfone, butyl sulfone, methyl methanesulfonate, dimethyl sulfite, dimethyl sulfoxide, dimethylsulfate, 3-methyl-2-oxazolidinone, fluorinated cyclic carbonate, methylene methane disulfonate, methyl cyanoacetate. In certain examples, the solvent is acetonitrile. In certain examples, the solvent is butyronitrile. In certain examples, the solvent is glutaronitrile. In certain examples, the solvent is hexanenitrile. In certain examples, the solvent is fluoroacetonitrile. In certain examples, the solvent is nitroacetonitrile. In certain examples, the solvent is iso-butyronitrile. In certain examples, the solvent is ethoxyacetonitrile. In certain examples, the solvent is pentanenitrile. In certain examples, the solvent is propanenitrile. In certain examples, the solvent is succinonitrile. In certain examples, the solvent is adiponitrile. In certain examples, the solvent is malononitrile. In certain examples, the solvent is benzonitrile. In certain examples, the solvent is methoxyacetonitrile. In certain examples, the solvent is a combination of succinonitrile and adiponitrile. In certain examples, the solvent is a combination of succinonitrile and glutaronitrile.
In some examples, the electrochemical cell set forth herein includes a dinitrile solvent which includes a dinitrile represented by Formula (I):
Figure US11342630-20220524-C00002
    • wherein:
    • R1, R2, R3, and R4 are, independently in each instance, selected from —CN, —NO2, —CO2, —SO4, —SO3, —SO2, —H, —CH2—SO3, —CHF—SO3, —CF2—SO3, —F, —Cl, —Br, and —I; and
    • subscript m is an integer from 1 to 1000.
In some of the examples herein, R1, R2, R3, and R4 are, independently in each instance, —H or —CN.
In some of the examples herein, R1, R2, R3, and R4 are, independently in each instance, —H or —NO2.
In some of the examples herein, R1, R2, R3, and R4 are, independently in each instance, —H or —CO2.
In some of the examples herein, R1, R2, R3, and R4 are, independently in each instance, —H or —SO4. In some of the examples herein, R1, R2, R3, and R4 are, independently in each instance, —H or —SO3. In some of the examples herein, R1, R2, R3, and R4 are, independently in each instance, —H or —SO2.
In some of the examples herein, R1, R2, R3, and R4 are, independently in each instance, —H or —CH2—SO3.
In some of the examples herein, R1, R2, R3, and R4 are, independently in each instance, —H or —CHF—SO3.
In some of the examples herein, R1, R2, R3, and R4 are, independently in each instance, —H or —CF2—SO3.
In some of the examples herein, R1, R2, R3, and R4 are, independently in each instance, —H or —F.
In some of the examples herein, R1, R2, R3, and R4 are, independently in each instance, —H or —Cl.
In some of the examples herein, R1, R2, R3, and R4 are, independently in each instance, —H or —Br.
In some of the examples herein, R1, R2, R3, and R4 are, independently in each instance, —H or —I.
In some examples herein, the catholyte solvent includes a member selected from the group consisting of:
Figure US11342630-20220524-C00003

and combinations thereof. In certain examples, the solvent is a combination of succinonitrile and adiponitrile. In certain examples, the solvent is a combination of succinonitrile and glutaronitrile.
In some examples herein, the catholyte solvent includes an organic sulfur-including solvent. In some examples herein, the organic sulfur-including solvent is selected from the group consisting of ethyl methyl sulfone, dimethyl sulfone, sulfolane, allyl methyl sulfone, butadiene sulfone, butyl sulfone, methyl methanesulfonate, and dimethyl sulfite.
In some of these examples, the lithium salt is selected from LiPF6, LiBOB, LiTFSi, LiFSI, LiAsF6, LiClO4, LiI, LiBF4, and a combination thereof. In certain examples, the lithium salt is LiPF6, In certain examples, the lithium salt is LiBOB. In certain examples, the lithium salt is LiTFSi. In certain examples, the lithium salt is LiBF4. In certain examples, the lithium salt is LiClO4. In certain examples, the lithium salt is LiFSI. In certain examples, the lithium salt is LiAsF6. In certain examples, the lithium salt is LiClO4. In certain examples, the lithium salt is LiI. In certain examples, the lithium salt is LiBF4.
In the examples herein, the catholyte is chemically stable when in contact with a solid separator.
In some of the examples herein, the electrochemical cell further includes a bonding layer which includes a solvent selected from ethylene carbonate (EC), diethylene carbonate, diethyl carbonate, dimethyl carbonate (DMC), ethyl-methyl carbonate (EMC), tetrahydrofuran (THF), γ-Butyrolactone (GBL), fluoroethylene carbonate (FEC), fluoromethyl ethylene carbonate (FMEC), trifluoroethyl methyl carbonate (F-EMC), fluorinated 3-(1,1,2,2-tetrafluoroethoxy)-1,1,2,2-tetrafluoropropane (i.e., 1,1,2,2-tetrafluoro-3-(1,1,2,2-tetrafluoroethoxy)propane (F-EPE)), fluorinated cyclic carbonate (F-AEC), propylene carbonate (PC), dioxolane, acetonitrile (ACN), succinonitrile, adiponitrile, hexanedinitrile, pentanedinitrile, acetophenone, isophorone, benzonitrile, dimethyl sulfate, dimethyl sulfoxide (DMSO) ethyl-methyl carbonate, ethyl acetate, methyl butyrate, dimethyl ether (DME), diethyl ether, propylene carbonate, dioxolane, glutaronitrile, gamma butyrolactone, and combinations thereof. In some examples, the solvent is ethylene carbonate (EC). In some examples, the solvent is diethylene carbonate. In some examples, the solvent is dimethyl carbonate (DMC). In some examples, the solvent is ethyl-methyl carbonate (EMC). In some examples, the solvent is tetrahydrofuran (THF). In some examples, the solvent is γ-Butyrolactone (GBL). In some examples, the solvent is fluoroethylene carbonate (FEC). In some examples, the solvent is fluoromethyl ethylene carbonate (FMEC). In some examples, the solvent is trifluoroethyl methyl carbonate (F-EMC). In some examples, the solvent is fluorinated 3-(1,1,2,2-tetrafluoroethoxy)-1,1,2,2-tetrafluoropropane (i.e., 1,1,2,2-tetrafluoro-3-(1,1,2,2-tetrafluoroethoxy)propane (F-EPE)). In some examples, the solvent is fluorinated cyclic carbonate (F-AEC). In some examples, the solvent is propylene carbonate (PC). In some examples, the solvent is dioxolane. In some examples, the solvent is acetonitrile (ACN). In some examples, the solvent is succinonitrile. In some examples, the solvent is adiponitrile/hexanedinitrile. In some examples, the solvent is acetophenone. In some examples, the solvent is isophorone. In some examples, the solvent is benzonitrile. In some examples, the solvent is dimethyl sulfate. In some examples, the solvent is dimethyl sulfoxide (DMSO). In some examples, the solvent is ethyl acetate. In some examples, the solvent is methyl butyrate. In some examples, the solvent is dimethyl ether (DME). In some examples, the solvent is diethyl ether. In some examples, the solvent is dioxolane. In some examples, the solvent is glutaronitrile. In some examples, the solvent is gamma butyrolactone. In some examples, the solvent is a combination of any solvents mentioned above. This bonding layer may be used to adhere or bond the cathode to the solid separator.
In some of the examples herein, the electrochemical cell further includes a bonding layer which includes a lithium salt in the bonding layer is selected from LiPF6, LiBOB, LFTSi, or combinations thereof. In certain examples, the lithium salt in the bonding layer is LiPF6 at a concentration of 0.5 M to 2 M. In certain examples, wherein the lithium salt in the bonding layer is LiTFSI at a concentration of 0.5 M to 2 M.
In some of the examples herein, the catholyte solvent is a solvent having a permittivity of greater than 30. In certain of these examples, the catholyte solvent is a dinitrile-containing solvent.
In some of the examples herein, the catholyte solvent is a solvent having a viscosity of greater than 0.01 cP and less than 10 cP at 25° C.
In some of the examples herein, the catholyte solvent is a solvent having a flash point of greater than 50° C. and less than 400° C.
In some of the examples herein, the catholyte solvent is a solvent having a melting point higher than −50° C. and lower than 30° C.
In some of the examples herein, the catholyte solvent is a solvent having a boiling point of greater than 80° C.
In some of the examples herein, the catholyte solvent is a solvent having a HOMO level of more than 7.2 eV below the vacuum level as calculated by DFT (density fuctional theory) with a B3LYP (Becke, 3-parameter, Lee-Yang-Parr) exchange-correlation functional and 6-311++G** basis set. In some examples, the HOMO level is more than 7.8 eV below the vacuum level as calculated by DFT with a B3LYP exchange-correlation functional and 6-311++G** basis set. In some examples, the HOMO level is more than 8.2 eV below the vacuum level as calculated by DFT with a B3LYP exchange-correlation functional and 6-311++G** basis set. For example, for succinonitrile, the HOMO=−9.65 eV, and LUMO=−0.92 eV; for ethyl methyl sulfone HOMO=−8.08 eV, LUMO=−0.62 eV.
In some of the examples herein, the catholyte solvent is a solvent is polar and aprotic.
In some of the examples herein, the catholyte has a lithium transference number of greater than 0.2.
In some of the examples herein, the catholyte has a total ionic conductivity of greater than 1e-4 S/cm at 25° C.
In some of the examples herein, the catholyte solvent has a vapor pressure of lower than 2 Torr at 20° C. In some of the examples herein, the catholyte solvent has a vapor pressure of lower than 0.2 Torr at 20° C. In some of the examples herein, the catholyte solvent has a vapor pressure of lower than 2e-2 Torr at 20° C.
In some of the examples herein, the catholyte solvent has a boiling point of greater than 80° C.
In some of the examples herein, the catholyte solvent has a boiling point of greater than 250° C.
In some of the examples herein, the catholyte solvent has a viscosity of less than 10 centipoise (cP) at 25° C.
In some of the examples herein, the catholyte further comprises a carbonate solvent in addition to the nitrile or dinitrile solvent. In some examples, the catholyte further comprises a solvent selected from ethylene carbonate (EC), diethylene carbonate, diethyl carbonate, dimethyl carbonate (DMC), ethyl-methyl carbonate (EMC), tetrahydrofuran (THF), γ-Butyrolactone (GBL), fluoroethylene carbonate (FEC), fluoromethyl ethylene carbonate (FMEC), trifluoroethyl methyl carbonate (F-EMC), fluorinated 3-(1,1,2,2-tetrafluoroethoxy)-1,1,2,2-tetrafluoropropane/1,1,2,2-tetrafluoro-3-(1,1,2,2-tetrafluoroethoxy)propane (F-EPE), fluorinated cyclic carbonate (F-AEC), propylene carbonate (PC), dioxolane, acetonitrile (ACN), succinonitrile, malononitrile, hexanedinitrile (adiponitrile), pentanedinitrile (glutaronitrile), acetophenone, isophorone, benzonitrile, dimethyl sulfate, dimethyl sulfoxide (DMSO) ethyl-methyl carbonate, ethyl acetate, methyl butyrate, dimethyl ether (DME), diethyl ether, propylene carbonate, dioxolane, glutaronitrile, gamma butyrolactone, or combinations thereof. In some of the examples herein, the catholyte further comprises a carbonate solvent in addition to the organic sulfur-including solvent. In some examples, the catholyte comprises organic sulfur-including solvent and ethylene carbonate in a ratio of about 1:9, 2:8, 3:7, 4:6, 5:5, 6:4, 7:3, 8:2, or 9:1.
In some of the examples herein, the catholyte solvent is stable up to 4.7V v. Lithium. In some of the examples herein, the catholyte solvent is stable up to 4.5V v. Lithium. In some of the examples herein, the catholyte solvent is stable up to 4.4V v. Lithium. In some examples herein, the catholyte solvent is stable up to 4.2V v. Lithium.
In some of the examples herein, the catholyte solvent is stable down to 1.5V.
In some of the examples herein, the catholyte solvent includes a nitrile represented by Formula (I):
Figure US11342630-20220524-C00004

wherein:
    • R1, R2, R3, and R4 are, independently in each instance, selected from —CN, —NO2, —CO2, —SO4, —SO3, —SO2, —CH2—SO3, —CHF—SO3, —CF2—SO3, —H, —F, —Cl, —Br, and —I;
    • and wherein subscript m is an integer from 1 to 1000.
In some of the examples herein, R1, R2, R3, and R4 are, independently in each instance, —H or —CN.
In some of the examples herein, R1, R2, R3, and R4 are, independently in each instance, —H or —NO2.
In some of the examples herein, R1, R2, R3, and R4 are, independently in each instance, —H or —CO2.
In some of the examples herein, R1, R2, R3, and R4 are, independently in each instance, —H or —SO4. In some of the examples herein, R1, R2, R3, and R4 are, independently in each instance, —H or —SO3. In some of the examples herein, R1, R2, R3, and R4 are, independently in each instance, —H or —SO2.
In some of the examples herein, R1, R2, R3, and R4 are, independently in each instance, —H or —CH2—SO3.
In some of the examples herein, R1, R2, R3, and R4 are, independently in each instance, —H or —CHF—SO3.
In some of the examples herein, R1, R2, R3, and R4 are, independently in each instance, —H or —CF2—SO3.
In some of the examples herein, R1, R2, R3, and R4 are, independently in each instance, —H or —F.
In some of the examples herein, R1, R2, R3, and R4 are, independently in each instance, —H or —Cl.
In some of the examples herein, R1, R2, R3, and R4 are, independently in each instance, —H or —Br.
In some of the examples herein, R1, R2, R3, and R4 are, independently in each instance, —H or —I.
In certain examples, subscript m is an integer from 1 to 1000. In some of the examples, subscript m is an integer from 1 to 100. In some of the examples, subscript m is an integer from 1 to 10. In some of the examples, subscript m is an integer from 1 to 5. In some of the examples, subscript m is an integer from 1 to 4. In some of the examples, subscript m is an integer from 1 to 3. In some of the examples, subscript m is an integer from 1 to 2. In some of the examples, subscript m is 1.
In certain other examples, subscript m is 1. In certain other examples, subscript m is 2. In certain other examples, subscript m is 3. In certain other examples, subscript m is 4. In certain other examples, subscript m is 5. In certain other examples, subscript m is 6. In certain other examples, subscript m is 7. In certain other examples, subscript m is 8. In certain other examples, subscript m is 9. In certain other examples, subscript m is 10. In certain other examples, subscript m is 11. In certain other examples, subscript m is 12. In certain other examples, subscript m is 13. In certain other examples, subscript m is 14. In certain other examples, subscript m is 15. In certain other examples, subscript m is 16. In certain other examples, subscript m is 17. In certain other examples, subscript m is 18. In certain other examples, subscript m is 19. In certain other examples, subscript m is 20.
In some examples herein, the catholyte includes a solvent selected from the group consisting of
Figure US11342630-20220524-C00005

and combinations thereof. In some examples, the solvent includes both succinonitrile and glutaronitrile. In other examples, the solvent includes succinonitrile and adiponitrile.
In some examples, the dinitrile of Formula I has a total ionic conductivity of greater than 1e-4 S/cm at room temperature.
In some examples, the dinitrile is malononitrile, succinonitrile, glutaronitrile, hexanedinitrile (adipodinitrile), sebaconitrile, subernitrile, pimelonitrile, and dodecanedinitrile, phthalonitrile or cis/trans-1,2-dicyanocyclohexane, or combinations thereof.
In some examples, the lithium salt is selected from LiPF6, LiBH4, LiBOB, LiBETI, LiTFSi, LiBF4, LiClO4, LiFSI, LiAsF6, LiClO4, LiI, LiBF4, and combination thereof.
In some examples, the lithium salt is selected from LiPF6, LiBH4, LiBOB, LiBETI, LiBF4, LiAsF6, LIFSI, LiTFSI, LiClO4, and combinations thereof.
In some examples, the lithium salt is present in the dinitrile solvent at a concentration of about 5-20 mol %.
In some examples, a lithium salt is present in the dinitrile solvent at a concentration of about 12 mol %.
In some examples, the catholyte further comprises a carbonate solvent.
In some examples, the catholyte comprises LiBF4, LiCF3SO3, LiN(CF3SO2)2, or a combination thereof.
In some examples, the catholyte solvent is a combination as follows:
Figure US11342630-20220524-C00006

wherein coefficients X, Y, and Z refer to the respective molar amounts of each of acetonitrile, succinonitrile, and glutaronitrile. In some examples, X is 0, Y is 0.87 and Z is 0.13.
In some examples, the catholyte further includes LiBF4 or LiN(CF3SO2)2.
In some examples, the catholyte further includes an additives such as VC (vinylene carbonate), VEC (vinyl ethylene carbonate), succinic anhydride, PES (prop-1-ene, 1-3 sultone), tris(trimethylsilyl) phosphite, ethylene sulfate, PBF, TMS (1,3-propylene sulfate), methylene methanedisulfonate (MMDS), lithium nitrate, propylene sulfate, trimethoxyboroxine, FEC, combinations thereof, and the like.
In some examples, the catholyte further includes VC.
In some examples, the catholyte further includes VEC.
In some examples, the catholyte further includes succinic anhydride.
In some examples, the catholyte further includes PES.
In some examples, the catholyte further includes ethylene sulfate.
In some examples, the catholyte further includes PBF.
In some examples, the catholyte further includes TMS.
In some examples, the catholyte further includes propylene sulfate.
In some examples, the catholyte further includes trimethoxyboroxine.
In some examples, the catholyte further includes MMDS.
In some examples, the catholytes here are paired with, laminated to, adjoined, or bonded to a solid separator. In some examples, the solid separator is a Li conducting solid-state electrolyte material useful as the separator. Separator materials include those that are stable to lithium metal, including sulfides (Li2S—SiS2—LiX, Li2S—B2S3—LiX, Li2S—P2S5—LiX, Li2S—SnS2—LiX, Li2S-Al2S3—LiX, and combinations thereof), borohydrides (LiBH4—LiX, LiNH2—LiX, LiBH4—LiNH2—LiX, and combinations thereof), LiPON, Li-stuffed garnet, lithium-rich antiperovskite, or LISICON materials. In some examples, the separators is not stable in contact with metal lithium. In some examples, the separator is a perovskite (LLTO), a phosphate (LATP, LAGP), or a Li-β-Al2O3.
In addition to dinitrile materials, such as but not limited to, malononitrile, succinonitrile, glutaronitrile, hexanedinitrile (adiponitrile), sebaconitrile, suberonitrile, pimelonitrile, dodecanedinitrile, and the like), some catholyte solvents herein include polar solvents with nitrile functionalities such as acetonitrile, butyronitrile, benzonitrile, hexanenitrile, fluoroacetonitrile, nitroacetonitrile, ethoxyacetonitrile, pentanenitrile, propanenitrile, iso-butyronitrile, and the like. In some examples, solvents may also include aprotic liquids with electron withdrawing groups such as fluorine (FEC, F-AEC, F-EPE, F-EMC, TTE). In some examples, solvents may also include aprotic liquids with a low HOMO level as calculated by density functional theory (DFT). In some other examples, solvents may also include MMDS, methyl pivalate, 1,2 dioxane, and sulfolane. In some of these examples, the oxidative stability of the dinitrile is related to its HOMO. As the HOMO of the dinitrile decreases, or is a higher (less negative) value, it is easier to oxidize the solvent.
In some examples herein, the lithium salts may include those known in the art such as, but not limited to, LiPF6, LiBOB, LiBETI, LiBF4, LiAsF6, LiFSI, LiTFSI, LiClO4, and combinations thereof.
In some examples herein, the catholyte comprises 0.57:0.43 glutaronitrile:succinonitrile (mol/mol) and 7 mol % LiBF4.
In some examples herein, the catholyte comprises 0.3:0.7 ethylene carbonate:sulfolane (v/v) and 1 M LiPF6.
D. Electrochemical Devices
In some examples, set forth herein is an electrochemical cell which includes a catholyte set forth herein.
In some examples, set forth herein is an electrochemical cell which includes a catholyte set forth herein which includes a dinitrile solvent and a lithium salt.
In some examples, set forth herein is an electrochemical cell which includes a catholyte set forth herein which includes a nitrile solvent and a lithium salt.
In some examples, set forth herein is an electrochemical cell which includes a catholyte set forth herein which includes an organic sulfur-including solvent and a lithium salt.
In some examples, set forth herein is an electrochemical cell, which includes a lithium metal negative electrode, a solid separator, and a positive electrode. In these examples, the positive electrode includes an active material, and a catholyte. In these examples, the catholyte includes a dinitrile solvent and a lithium salt.
In some examples, the lithium metal negative electrode is a layer laminated to the solid separator, wherein the solid separator is a layer laminated to the positive electrode.
In some examples, the lithium metal negative electrode is laminated to the solid separator, wherein the solid separator is laminated to the positive electrode.
In some examples, the lithium metal negative electrode is formed in situ.
In some examples, solid separator is impermeable to the catholyte. In these examples, the solid separator is dense enough or the catholyte is viscous enough such that the catholyte does not penetrate through the solid separator. In some of these examples, the solid separator protects or encapsulates the lithium metal negative electrode and prevents it from contacting the dinitrile catholyte.
In some examples, the electrochemical cell includes a bonding layer between the positive electrode and the solid separator. In some examples, the bonding layer comprises a solvent and a lithium salt. In some examples, the solvent in the bonding layer is selected from the group consisting of ethylene carbonate, methylene carbonate, methyl ethyl carbonate, diethylene carbonate.
In some examples, the electrochemical cell includes a lithium salt selected from LiPF6, LiBOB, LiTFSi, LiBF4, LiClO4, LiAsF6, LiFSI, LiClO4, Li, and a combination thereof.
In certain examples, the bonding layer further comprises a polymer selected from the group consisting of polyacrylonitrile (PAN), polypropylene, polyethylene oxide (PEO), polymethyl methacrylate (PMMA), polyvinyl chloride (PVC), polyvinyl pyrrolidone (PVP), polyethylene oxide poly(allyl glycidyl ether) PEO-AGE, polyethylene oxide 2-methoxyethoxy)ethyl glycidyl ether (PEO-MEEGE), polyethylene oxide 2-methoxyethoxy)ethyl glycidyl poly(allyl glycidyl ether) (PEO-MEEGE-AGE), polysiloxane, polyvinylidene fluoride (PVdF), polyvinylidene fluoride hexafluoropropylene (PVdF-HFP), and rubbers such as ethylene propylene (EPR), nitrile rubber (NPR), styrene-butadiene-rubber (SBR), polybutadiene polymer, polybutadiene rubber (PB), polyisobutadiene rubber (PIB), polyisoprene rubber (PI), polychloroprene rubber (CR), acrylonitrile-butadiene rubber (NBR), polyethyl acrylate (PEA), polyvinylidene fluoride (PVDF), and polyethylene (e.g., low density linear polyethylene). In some examples, the polymer in the bonding layer is polyacrylonitrile (PAN) or polyvinylidene fluoride hexafluoropropylene (PVdF-HFP). In some examples, the polymer in the bonding layer is selected from the group consisting of PAN, PVdF-HFP, PVDF-HFP and PAN, PMMA, PVC, PVP, PEO, and combinations thereof. In certain examples, the polymer is polyacrylonitrile (PAN). In certain examples, the polymer is polypropylene. In certain examples, the polymer is polyethylene oxide (PEO). In certain examples, the polymer is polymethyl methacrylate (PMMA). In certain examples, the polymer is polyvinyl chloride (PVC). In certain examples, the polymer is polyvinyl pyrrolidone (PVP). In certain examples, the polymer is polyethylene oxide poly(allyl glycidyl ether) PEO-AGE. In certain examples, the polymer is polyethylene oxide 2-methoxyethoxy)ethyl glycidyl ether (PEO-MEEGE). In certain examples, the polymer is polyethylene oxide 2-methoxyethoxy)ethyl glycidyl poly(allyl glycidyl ether) (PEO-MEEGE-AGE). In certain examples, the polymer is polysiloxane. In certain examples, the polymer is polyvinylidene fluoride (PVDF). In certain examples, the polymer is polyvinylidene fluoride hexafluoropropylene (PVdF-HFP). In certain examples, the polymer is a rubber such as ethylene propylene (EPR), nitrile rubber (NPR), styrene-butadiene-rubber (SBR), polybutadiene polymer, polybutadiene rubber (PB), polyisobutadiene rubber (PIB), polyisoprene rubber (PI), polychloroprene rubber (CR), acrylonitrile-butadiene rubber (NBR), and polyethyl acrylate (PEA). In some examples, the polymer is polyethylene (e.g., low density linear polyethylene). In some examples, the polymer is a combination of any polymers mentioned above. In some examples, the solvent in the bonding layer is selected from ethylene carbonate (EC), diethylene carbonate, diethyl carbonate, dimethyl carbonate (DMC), ethyl-methyl carbonate (EMC), tetrahydrofuran (THF), γ-Butyrolactone (GBL), fluoroethylene carbonate (FEC), fluoromethyl ethylene carbonate (FMEC), trifluoroethyl methyl carbonate (F-EMC), fluorinated 3-(1,1,2,2-tetrafluoroethoxy)-1,1,2,2-tetrafluoropropane/1,1,2,2-tetrafluoro-3-(1,1,2,2-tetrafluoroethoxy)propane (F-EPE), fluorinated cyclic carbonate (F-AEC), propylene carbonate (PC), dioxolane, acetonitrile (ACN), succinonitrile, adiponitrile (hexanedinitrile), glutaronitrile (pentanedinitrile), acetophenone, isophorone, benzonitrile, dimethyl sulfate, dimethyl sulfoxide (DMSO) ethyl-methyl carbonate, ethyl acetate, methyl butyrate, dimethyl ether (DME), diethyl ether, propylene carbonate, dioxolane, gamma butyrolactone, or combinations thereof. In some of these examples, the solvent in the bonding layer is a 1:1 w/w mixture of EC:PC. In some of these examples, the lithium salt in the bonding layer is selected from LiPF6, LiBOB, LFTSi, or combinations thereof. In some of these examples, the lithium salt in the bonding layer is LiPF6 at a concentration of 0.5 M to 2M. In some of these examples, the lithium salt in the bonding layer is LiTFSI at a concentration of 0.5 M to 2M. In some of these examples, the lithium salt in the bonding layer is present at a concentration from 0.01 M to 10 M.
In some of these examples, the solid separator is selected from a lithium sulfide, a lithium borohydride, a LiPON, a lithium-stuffed garnet, a lithium-rich antiperovskite, a LISICON, and a combination thereof. In certain examples, the solid separator is an oxide selected from a lithium-stuffed garnet characterized by the formula LixLayZrzOt.qAl2O3, wherein 4<x<10, 1<y<4, 1<z<3, 6<t<14, 0≤q≤1.
In some of these examples, the solid separator is a lithium-stuffed garnet doped with Al, Nb, Ga, and/or Ta.
In some of these examples, the solid separator is a lithium-stuffed garnet characterized by LiaLabZrcAldMe″eOf, wherein 5<a<8.5; 2<b<4; 0<c≤2.5; 0≤d<2; 0≤e<2, and 10<f<13 and Me″ is a metal selected from Nb, Ga, Ta, or combinations thereof.
In some examples, the lithium-stuffed garnet is characterized by the formula LixLayZrzOt.0.11(Al2O3) or LixLayZrzOt.(Al2O3), wherein 5<x<8.5.
In some of these examples, the solid separator is a sulfide or sulfide-halide is selected from LPSI, LSS, SLOPS, LSTPS, SLOBS, and LATS.
In some of these examples, the separator is a sulfide or sulfide-halide is selected from LiBHI, LiBNHI, LiBHCl, LiBNHCl, LiBHBr, LiBNHBr, and combinations thereof.
In some of these examples, the solid separator is a thin film.
In some of these examples, the solid separator is a monolith.
In some of these examples, the solid separator is a composite of a polymer and a solid electrolyte.
In some of these examples, the catholyte solvent(s) is a solvent having a permittivity of greater than 30.
In some of these examples, the catholyte solvent(s) is a solvent having a viscosity of less than 10 cP at 25° C.
In some of these examples, the catholyte solvent(s) is a solvent having a flash point of greater than 50° C.
In some of these examples, the catholyte solvent(s) is a solvent having a melting point of lower than 30° C.
In some of these examples, the catholyte solvent(s) is a solvent having a boiling point of greater than 80° C.
In some of these examples, the catholyte solvent(s) is a solvent having a HOMO level of more than 7.2 eV below the vacuum level.
In some of these examples, the catholyte solvent(s) is polar and aprotic. In some of these example, the nitrile solvent is selected from acetonitrile, butyronitrile, benzonitrile, hexanenitrile, fluoroacetonitrile, nitroacetonitrile, malononitrile, ethoxyacetonitrile, pentanenitrile, propanenitrile, and iso-butyronitrile. In some of these example, the dinitrile solvent comprises a member selected from the group consisting of fluoroethylene carbonate (FEC), fluoromethyl ethylene carbonate (FMEC), trifluoroethyl methyl carbonate (F-EMC), fluorinated 3-(1,1,2,2-tetrafluoroethoxy)-1,1,2,2-tetrafluoropropane (i.e., 1,1,2,2-tetrafluoro-3-(1,1,2,2-tetrafluoroethoxy)propane (F-EPE)), fluorinated cyclic carbonate (F-AEC), and TTE. In some of these example, the dinitrile solvent comprises a member selected from the group consisting of MMDS, methyl pivalate, 1,2 dioxane, sulfolane, and combinations thereof.
In some examples, the catholyte has a lithium transference number of greater than 0.2.
In some examples, the catholyte has a total ionic conductivity of greater than 1e-4 S/cm at 25° C.
In some examples, the catholyte solvent has a vapor pressure of lower than 2e-2 Torr at 20° C., or lower than 0.2 Torr at 20° C., or lower than 2 Torr at 20° C.
In some examples, the catholyte solvent has a boiling point of greater than 80° C.
In some examples, the catholyte solvent has a boiling point of greater than 250° C.
In some examples, the catholyte solvent has a viscosity of less than 10 centipoise (cP) at 25° C.
In some examples, the catholyte further comprises a carbonate solvent. In some of these examples, the catholyte further comprises a solvent selected from ethylene carbonate (EC), diethylene carbonate, diethyl carbonate, dimethyl carbonate (DMC), ethyl-methyl carbonate (EMC), tetrahydrofuran (THF), γ-Butyrolactone (GBL), fluoroethylene carbonate (FEC), fluoromethyl ethylene carbonate (FMEC), trifluoroethyl methyl carbonate (F-EMC), fluorinated 3-(1,1,2,2-tetrafluoroethoxy)-1,1,2,2-tetrafluoropropane/1,1,2,2-Tetrafluoro-3-(1,1,2,2-tetrafluoroethoxy)propane (F-EPE), fluorinated cyclic carbonate (F-AEC), propylene carbonate (PC), dioxolane, acetonitrile (ACN), succinonitrile, adiponitrile, hexanedinitrile, pentanedinitrile, acetophenone, isophorone, benzonitrile, dimethyl sulfate, dimethyl sulfoxide (DMSO), ethyl acetate, methyl butyrate, dimethyl ether (DME), diethyl ether, propylene carbonate, dioxolane, glutaronitrile, and combinations thereof.
In some examples, the catholyte solvent is stable up to 4.7V v. Lithium. In some examples, the catholyte solvent is stable up to 4.5V v. Lithium. In some examples, the catholyte solvent is stable up to 4.4V v. Lithium.
In some examples, the catholyte solvent is stable towards the solid separator.
In some examples, the catholyte solvent is stable down to 1.5V.
In some examples, the dinitrile solvent is stable up to 4.7V v. Lithium.
In some examples, the dinitrile solvent is stable towards the solid separator.
In some examples, the dinitrile solvent is stable down to 1.5V.
In some examples herein, the dinitrile of Formula I has a total ionic conductivity of greater than 1e-4 S/cm at room temperature.
In some examples herein, the electrochemical cell has a cyclability wherein greater than 70% of the initial energy remains at cycle 100 when cycled at a C/3 rate at 30° C.
In some examples herein, the electrochemical cell has a lifetime wherein greater than 70% of the initial energy remains at cycle 100 when cycled at a C/3 rate at 30° C.
In some examples herein, the electrochemical cell has a rate performance wherein greater than 70% of the initial power capability at 50% state-of-charge (SOC) remains at cycle 100 when cycled at a C/3 rate at 30° C.
In some examples herein, the electrochemical cell has an oxidation potential wherein greater than 70% of the initial energy remains at cycle 100 when cycled at a C/3 rate at 30° C.
In some examples herein, the electrochemical cell has an impedance at cycle 100 less than 13% of the initial impedance when cycled at a C/3 rate at 30° C.
In any of the electrochemical cells described herein, the dinitrile may be selected from malononitrile, succinonitrile, glutaronitrile, hexanedinitrile/adiponitrile, sebaconitrile, subemitrile, pimelonitrile, and dodecanedinitrile, phthalonitrile or cis/trans-1,2-dicyanocyclohexane, and combinations thereof.
In any of the electrochemical cells described herein, the lithium salt may be selected from LiPF6, LiBH4, LiBOB, LiBETI, LiTFSi, LiClO4, LiAsF6, LiFSI, LiClO4, LiI, LiBF4, and combination thereof.
In any of the electrochemical cells described herein, the lithium salt may be selected from LiPF6, LiBH4, LiBOB, LiBETI, LiBF4, LiAsF6, LIFSI, LiTFSI, LiClO4, and combinations thereof.
In some examples, the lithium salt is present in the dinitrile solvent at a concentration of about 5-20 mol %.
In some examples, the lithium salt is present in the dinitrile solvent at a concentration of about 12 mol %.
In some examples, the solid separator is a lithium-stuffed-garnet, an LiBHI, Li3N, a lithium-sulfides, a LiPON, a LISON, or a combination thereof.
In some examples, the active material is selected from a nickel manganese cobalt oxide (NMC), a nickel cobalt aluminum oxide (NCA), Li(NiCoAl)O2, a lithium cobalt oxide (LCO), a lithium manganese cobalt oxide (LMCO), a lithium nickel manganese cobalt oxide (LMNCO), a lithium nickel manganese oxide (LNMO), Li(NiCoMn)O2, LiMn2O4, LiCoO2, LiMn2-aNiaO4, wherein a is from 0 to 2, or LiMPO4, wherein M is Fe, Ni, Co, or Mn.
In some examples, the active material is selected from FeF2, NiF2, FeOxF3-2x, FeF3, MnF3, CoF3, CuF2 materials, alloys thereof, and combinations thereof
In some examples, the catholyte herein further includes a carbonate solvent.
In some examples, the catholyte includes LiBF4, LiCF3SO3, LiN(CF3SO2)2, or a combination thereof.
In some examples, the dinitrile is a combination as follows:
Figure US11342630-20220524-C00007
    • wherein coefficients X, Y, and Z refer to the respective molar amounts of each of acetonitrile, succinonitrile, and glutaronitrile.
      In some of these examples, X is 0, Y is 0.87 and Z is 0.13.
In some examples, the electrochemical cell herein includes LiBF4 or LiN(CF3SO2)2.
In some examples, the electrochemical cell herein includes a solid separator which includes a lithium-stuffed garnet oxide characterized by the formula LiuLavZrxOy.zAl2O3, wherein
    • u is a rational number from 4 to 8;
    • v is a rational number from 2 to 4;
    • x is a rational number from 1 to 3;
    • y is a rational number from 10 to 14;
    • z is a rational number from 0.05 to 1; and
    • wherein u, v, x, y, and z are selected so that the lithium-stuffed garnet oxide is charge neutral.
In some examples of the above formula, u is selected from 4, 5, 6, 7, and 8; v is selected from 2, 3, and 4; x is selected from 1, 2, and 3; y is selected from 10, 11, 12, 13, and 14; and z is selected from 0.05, 0.1, 0.15, 0.2, 0.25, 0.3, 0.35, 0.4, 0.45, 0.5, 0.55, 0.6, 0.65, 0.7, 0.75, 0.8, 0.85, 0.9, 0.95, and 1.
In some examples, the electrochemical cell herein includes a solid separator which includes a lithium sulfide characterized by one of the following Formula:
    • LiaSibSncPdSeOf, wherein 2≤a≤8, b+c=1, 0.5≤d≤2.5, 4≤e≤12, and 0<f≤10;
    • LigAshSnjSkOl, wherein 2≤g≤6, 0≤h≤1, 0≤j≤1, 2≤k≤6, and 0≤l≤10;
    • LimPnSpIq, wherein 2≤m≤6, 0≤n≤1, 0≤p≤1, 2≤q≤6; or
    • a mixture of (Li2S):(P2S5) having a molar ratio from about 10:1 to about 6:4 and LiI, wherein the ratio of [(Li2S):(P2S5)]:LiI is from 95:5 to 50:50;
    • a mixture of LiI and Al2O3;
    • Li3N;
    • LPS+X, wherein X is selected from Cl, I, or Br;
    • vLi2S+wP2S5+yLiX;
    • vLi2S+wSiS2+yLiX;
    • vLi2S+wB2S3+yLiX;
    • a mixture of LiBH4 and LiX wherein X is selected from Cl, I, or Br; or
    • vLiBH4+wLiX+yLiNH2, wherein X is selected from Cl, I, or Br; and
    • wherein coefficients v, w, and y are rational numbers from 0 to 1.
In some examples, the electrochemical cell herein includes a solid separator which includes a lithium-stuffed garnet oxide characterized by the formula LiuLavZrxOy.zTa2O5, wherein
    • u is a rational number from 4 to 10;
    • v is a rational number from 2 to 4;
    • x is a rational number from 1 to 3;
    • y is a rational number from 10 to 14; and
    • z is a rational number from 0 to 1;
    • wherein u, v, x, y, and z are selected so that the lithium-stuffed garnet oxide is charge neutral.
In some examples of the above formula, u is selected from 4, 5, 6, 7, 8, 9, and 10; v is selected from 2, 3, and 4; x is selected from 1, 2, and 3; y is selected from 10, 11, 12, 13, and 14; and z is selected from 0, 0.05, 0.1, 0.15, 0.2, 0.25, 0.3, 0.35, 0.4, 0.45, 0.5, 0.55, 0.6, 0.65, 0.7, 0.75, 0.8, 0.85, 0.9, 0.95, and 1.
In some examples, the electrochemical cell herein includes a solid separator which includes a lithium-stuffed garnet oxide characterized by the formula LiuLavZrxOy.zNb2O5, wherein
    • u is a rational number from 4 to 10;
    • v is a rational number from 2 to 4;
    • x is a rational number from 1 to 3;
    • y is a rational number from 10 to 14; and
    • z is a rational number from 0 to 1;
    • wherein u, v, x, y, and z are selected so that the lithium-stuffed garnet oxide is charge neutral.
In some examples of the above formula, u is selected from 4, 5, 6, 7, 8, 9, and 10; v is selected from 2, 3, and 4; x is selected from 1, 2, and 3; y is selected from 10, 11, 12, 13, and 14; and z is selected from 0, 0.05, 0.1, 0.15, 0.2, 0.25, 0.3, 0.35, 0.4, 0.45, 0.5, 0.55, 0.6, 0.65, 0.7, 0.75, 0.8, 0.85, 0.9, 0.95, and 1.
In some examples, the electrochemical cell herein include a solid separator which includes a lithium-stuffed garnet oxide characterized by the formula LiuLavZrxOy.z Ga2O3, wherein
    • u is a rational number from 4 to 10;
    • v is a rational number from 2 to 4;
    • x is a rational number from 1 to 3;
    • y is a rational number from 10 to 14; and
    • z is a rational number from 0 to 1;
    • wherein u, v, x, y, and z are selected so that the lithium-stuffed garnet oxide is charge neutral.
In some examples of the above formula, u is selected from 4, 5, 6, 7, 8, 9, and 10; v is selected from 2, 3, and 4; x is selected from 1, 2, and 3; y is selected from 10, 11, 12, 13, and 14; and z is selected from 0, 0.05, 0.1, 0.15, 0.2, 0.25, 0.3, 0.35, 0.4, 0.45, 0.5, 0.55, 0.6, 0.65, 0.7, 0.75, 0.8, 0.85, 0.9, 0.95, and 1.
In some examples, the electrochemical cell herein includes a solid separator which includes a lithium-stuffed garnet oxide characterized by the formula LiuLavZrxOy.zTa2O5 bAl2O3, wherein
    • u is a rational number from 4 to 10;
    • v is a rational number from 2 to 4;
    • x is a rational number from 1 to 3;
    • y is a rational number from 10 to 14;
    • z is a rational number from 0 to 1;
    • b is a rational number from 0 to 1; and
    • wherein z+b≤1
In some examples of the above formula, u is selected from 4, 5, 6, 7, 8, 9, and 10; v is selected from 2, 3, and 4; x is selected from 1, 2, and 3; y is selected from 10, 11, 12, 13, and 14; and z and b are each independently selected from 0, 0.05, 0.1, 0.15, 0.2, 0.25, 0.3, 0.35, 0.4, 0.45, 0.5, 0.55, 0.6, 0.65, 0.7, 0.75, 0.8, 0.85, 0.9, 0.95, and 1.
In some examples, the electrochemical cell herein includes a solid separator which includes a lithium-stuffed garnet oxide characterized by the formula LiuLavZrxOy.zNb2O5 bAl2O3, wherein
    • u is a rational number from 4 to 10;
    • v is a rational number from 2 to 4;
    • x is a rational number from 1 to 3;
    • y is a rational number from 10 to 14;
    • z is a rational number from 0 to 1;
    • b is a rational number from 0 to 1;
    • wherein z+b≤1; and
    • wherein u, v, x, y, and z are selected so that the lithium-stuffed garnet oxide is charge neutral.
In some examples of the above formula, u is selected from 4, 5, 6, 7, 8, 9, and 10; v is selected from 2, 3, and 4; x is selected from 1, 2, and 3; y is selected from 10, 11, 12, 13, and 14; and z and b are each independently selected from 0, 0.05, 0.1, 0.15, 0.2, 0.25, 0.3, 0.35, 0.4, 0.45, 0.5, 0.55, 0.6, 0.65, 0.7, 0.75, 0.8, 0.85, 0.9, 0.95, and 1.
In some examples, the electrochemical cell herein includes a solid separator which includes a lithium-stuffed garnet oxide characterized by the formula LiuLavZrxOy.z Ga2O3.bAl2O3, wherein
    • u is a rational number from 4 to 10;
    • v is a rational number from 2 to 4;
    • x is a rational number from 1 to 3;
    • y is a rational number from 10 to 14;
    • z is a rational number from 0 to 1; and
    • b is a rational number from 0 to 1;
    • wherein z+b≤1;
    • wherein u, v, x, y, and z are selected so that the lithium-stuffed garnet oxide is charge neutral.
In some examples, u is selected from 4, 5, 6, 7, 8, 9, and 10. In some examples, v is selected from 2, 3, and 4. In some examples, x is selected from 1, 2, and 3. In some examples, y is selected from 10, 11, 12, 13, and 14. In some examples, z and b are each independently selected from 0, 0.05, 0.1, 0.15, 0.2, 0.25, 0.3, 0.35, 0.4, 0.45, 0.5, 0.55, 0.6, 0.65, 0.7, 0.75, 0.8, 0.85, 0.9, 0.95, and 1.
In some examples, the electrochemical cell herein includes a positive electrode in direct contact with a solid electrolyte separator.
In some examples, the electrochemical cell herein includes catholyte which includes an additives such as VC (vinylene carbonate), VEC (vinyl ethylene carbonate), succinic anhydride, PES (prop-1-ene, 1-3 sultone), tris(trimethylsilyl) phosphite, ethylene sulfate, PBF, TMS (1,3-propylene sulfate), propylene sulfate, MMDS, trimethoxyboroxine, FEC, combinations thereof, and the like.
In some examples, the solid separator of the electrochemical cell is a thin and free standing sintered garnet film, wherein the film thickness is less than 50 μm and greater than 10 nm, wherein the film comprises a garnet characterized by the formula LixLa3Zr2O12.qAl2O3, wherein x ranges from 5.5 to 9; and q ranges from 0.05 to 1.0; and wherein the film is not adhered or fixed to a substrate. In some examples, the molar ratio of Al2O3:LixLa3Zr2O12, is 0.35, 0.5, 0.67 or 1.0. In some examples, the film has a surface roughness of less than 5 μm. In some examples, the garnet has a median grain size of between 0.1 μm and 10 μm. In some examples, the film has an area specific resistance (ASR) of less than 10 Ωcm2. In some examples, the film has an area specific resistance (ASR) of less than 10 Ωcm2 at 80° C. In some examples, the carbon content is less than 5 atomic %. In some examples, the film thickness is about 49 μm. In some examples, the solid separator of the electrochemical cell is a thin film comprising a lithium stuffed garnet and Al2O3, wherein the lithium-stuffed garnet is characterized by the empirical formula LixLayZrzOt, wherein 5.5<x<6.7, 1.5<y<4, 1≤z≤2, 10≤t≤13; and wherein the molar ratio of Al2O3:gamet is between 0.05 to 0.7; wherein the thin film has a film thickness of about 10 nm to about 100 μm; and wherein the thin film has grains having a d50 diameter between 100 nm and 10 μm. In some examples, the thin film is characterized by the empirical formula LixLa3Zr2O12.p½Al2O3; wherein 5.5<x<6.7 and 0.1<p<1.4. In some examples, the molar ratio of Al2O3:garnet is between 0.25 and 0.45. In some examples, the molar ratio of Al2O3:garnet is 0.35. In some examples, the film thickness is less than 50 μm and greater than 10 nm. In some examples, the thin film is a thin film monolith. In some examples, the thin film is a sintered thin film monolith. In some examples, the thin film has a density of about 4.5-5.2 g/cm3.
E. Methods of Making
In some examples, set forth herein is a method for making a catholyte set forth herein which includes a nitrile solvent and a lithium salt, wherein the method includes providing a nitrile solvent, providing a lithium salt, mixing the dinitrile solvent and the lithium salt to form a mixture, and optionally heating the mixture. In some examples, the nitrile solvent is a dinitrile solvent. In some examples, the nitrile solvent comprises or is selected from those solvents described above with respect to the catholyte of the present invention(s). In some examples, the nitrile solvent has the properties described above with respect to the catholyte of the present invention(s). In some examples, the lithium salt is selected from those lithium salts described above with respect to the catholyte of the present invention(s). In some examples, the nitrile solvent further comprises a solvent selected from those described above with respect to the catholyte of the present invention(s).
In some examples, set forth herein is a method for making a catholyte set forth herein which includes an organic sulfur-including solvent and a lithium salt, wherein the method includes providing an organic sulfur-including solvent, providing a lithium salt, mixing the organic sulfur-including solvent and the lithium salt to form a mixture, and optionally heating the mixture. In some examples, the method includes drying the solvent(s) and/or salts before or after mixing. In some examples, the drying comprises heating and/or processing the material with a desiccating or absorbing material.
F. Methods of Using
In some examples, set forth herein is a method of using an electrochemical cell, which is set forth herein, or using an electrochemical cell that includes a catholyte, which is set forth herein. In some of these methods, the methods include charging the electrochemical cell to a voltage greater than 4.3V. In some methods, the methods also include discharging the electrochemical cell to a voltage less than 4.3V.
In some examples, the methods herein include charging the battery to a voltage greater than 4.4V. In some examples, the methods herein include charging the battery to a voltage greater than 4.5V. In some examples, the methods herein include charging the battery to a voltage greater than 4.6V. In some examples, the methods herein include charging the battery to a voltage greater than 4.7V. In some examples, the methods herein include charging the battery to a voltage greater than 4.8V. In some examples, the methods herein include charging the battery to a voltage greater than 4.9V. In some examples, the methods herein include charging the battery to a voltage greater than 5.0V. In some examples, the methods herein include charging the battery to a voltage greater than 5.1V. In some examples, the methods herein include charging the battery to a voltage greater than 5.2V. In some examples, the methods herein include charging the battery to a voltage greater than 5.3V. In some examples, the methods herein include charging the battery to a voltage greater than 5.4V. In some examples, the methods herein include charging the battery to a voltage greater than 5.5V.
In some examples, the methods herein include charging the battery under pressure. In some examples, the pressure is about 50-300 pounds per square inch (PSI). In some examples, the pressure is about 50 PSI. In some examples, the pressure is about 60 PSI. In some examples, the pressure is about 70 PSI. In some examples, the pressure is about 80 PSI. In some examples, the pressure is about 90 PSI. In some examples, the pressure is about 100 PSI. In some examples, the pressure is about 110 PSI. In some examples, the pressure is about 120 PSI. In some examples, the pressure is about 130 PSI. In some examples, the pressure is about 140 PSI. In some examples, the pressure is about 150 PSI. In some examples, the pressure is about 160 PSI. In some examples, the pressure is about 170 PSI. In some examples, the pressure is about 180 PSI. In some examples, the pressure is about 190 PSI. In some examples, the pressure is about 200 PSI. In some examples, the pressure is about 210 PSI. In some examples, the pressure is about 220 PSI. In some examples, the pressure is about 230 PSI. In some examples, the pressure is about 240 PSI. In some examples, the pressure is about 250 PSI. In some examples, the pressure is about 260 PSI. In some examples, the pressure is about 270 PSI. In some examples, the pressure is about 280 PSI. In some examples, the pressure is about 290 PSI. In some examples, the pressure is about 300 PSI.
In some examples, the methods herein include discharging the battery under pressure. In some examples, the pressure is about 50-300 pounds per square inch (PSI). In some examples, the pressure is about 50 PSI. In some examples, the pressure is about 60 PSI. In some examples, the pressure is about 70 PSI. In some examples, the pressure is about 80 PSI. In some examples, the pressure is about 90 PSI. In some examples, the pressure is about 100 PSI. In some examples, the pressure is about 110 PSI. In some examples, the pressure is about 120 PSI. In some examples, the pressure is about 130 PSI. In some examples, the pressure is about 140 PSI. In some examples, the pressure is about 150 PSI. In some examples, the pressure is about 160 PSI. In some examples, the pressure is about 170 PSI. In some examples, the pressure is about 180 PSI. In some examples, the pressure is about 190 PSI. In some examples, the pressure is about 200 PSI. In some examples, the pressure is about 210 PSI. In some examples, the pressure is about 220 PSI. In some examples, the pressure is about 230 PSI. In some examples, the pressure is about 240 PSI. In some examples, the pressure is about 250 PSI. In some examples, the pressure is about 260 PSI. In some examples, the pressure is about 270 PSI. In some examples, the pressure is about 280 PSI. In some examples, the pressure is about 290 PSI. In some examples, the pressure is about 300 PSI.
In some examples, set forth herein method of storing an electrochemical cell, wherein the methods includes providing an electrochemical cell of any one of claims, wherein the an electrochemical cell has greater than 20% state-of-charge (SOC); and storing the battery for at least one day.
In some examples, the storing the battery is for at least two days.
In some examples, the storing the battery is for at least three days.
In some examples, the storing the battery is for at least four days.
In some examples, the storing the battery is for at least five days.
In some examples, the storing the battery is for at least six days.
In some examples, the storing the battery is for at least seven days.
In some examples, the storing the battery is for at least eight days.
In some examples, the storing the battery is for at least nine days.
In some examples, the storing the battery is for at least ten days.
In some examples, the storing the battery is for at least eleven days.
In some examples, the storing the battery is for at least twelve days.
In some examples, the storing the battery is for at least thirteen days.
In some examples, the storing the battery is for at least fourteen days.
In some examples, the storing the battery is for at least fifteen days.
In some examples, the storing the battery is for at least sixteen days.
In some examples, the storing the battery is for at least seventeen days.
In some examples, the storing the battery is for at least eighteen days.
In some examples, the storing the battery is for at least nineteen days.
In some examples, the storing the battery is for at least twenty days.
In some examples, the storing the battery is for at least twenty-one days.
In some examples, the storing the battery is for at least twenty-two days.
In some examples, the storing the battery is for at least twenty-three days.
In some examples, the storing the battery is for at least twenty-four days.
In some examples, the storing the battery is for at least twenty-five days.
In some examples, the storing the battery is for at least twenty-six days.
In some examples, the storing the battery is for at least twenty-seven days. [and 28, 29, and 30 days]
In some example, the storing the battery for at least one day is at a temperature greater than 20° C. In some other examples, the storing the battery for at least one day is at a temperature greater than 40° C.
In any of the methods, above, in some examples, the method further includes charging the battery to a voltage greater than 4.3V v. Li.
G. Examples
To record conductivity, a Biologic VMP3 was used. An electrochemical cell was constructed with blocking electrodes. A catholyte material was made as a gel and was used to fill the porosity of a porous separator such as a Celgard membrane or glass fiber separator. To record the mass fraction of electrolyte, a mass loss on drying tool such as an Arizona Instruments Computrac Max 5000XL #1 was used. Electrochemical cycling was performed with Arbin BT-G or BT-2043.
To record vapor pressure, Micromeritics BET tool was used.
Example 1—ASRdc of Nitrile and Carbonate Cathode Electrolytes
In this Example, the ASRdc increase in electrochemical cells stored at 4.6V and 45° C. was monitored for four weeks. Herein, ASRdc is the Area-specific resistance (area specific resistance), which is determined by measuring the difference in voltage from the end of a 30 minute current pulse to a steady state value after 10 minutes. This means that ASR was determined by measuring a voltage change and calculating ASR by the equation, ASR=ΔV/j where ΔV is the voltage change after a current pulse in a GITT (Galvanostatic intermittent titration technique) test and j is the current density applied to the cell in the GITT test.
One electrochemical cell included a cathode, layered with a gel electrolyte (i.e., catholyte), which was layered with a solid garnet separator, and to which the opposite side of the solid garnet separator was layered with Li metal by evaporation. The cell was maintained at a pressure of about 50-300 psi. The gel electrolyte included ethylene carbonate:ethyl-methyl-carbonate (EC:EMC) in a 3:7 w/w ratio+1M LiPF6 at 2 w/w FEC. The solid garnet separator is a pellet cell which can be prepared according to the methods disclosed in U.S. Provisional Application No. 62/544,724 filed Aug. 11, 2017, which is incorporated by reference herein in its entirety.
A second electrochemical cell included a cathode, layered with a electrolyte (i.e., catholyte), which was layered with a solid garnet separator, and to which the opposite side of the solid garnet separator was layered with Li metal by evaporation. The cell was maintained at a pressure of about 50-300 psi. The electrolyte included succinonitrile and 12 mol % LiBF4.
The two cells described in this Example were stored at high voltage (4.6V) at 45° C. and monitored for four weeks. After each week, each cell was discharged to measure the self-discharge, followed by a full charge-discharge at C/10, 2.7-4.5V, with 30 min pulses followed by 1 min rests to measure the ASR.
From this data, the ASR was calculated and the results are presented in FIGS. 2 and 3. Median charge and discharge ASRdc increased each week. It can be seen that the cell impedance growth was less for the cell with the nitrile catholyte compared to the cell with the carbonate electrolyte. The data also indicates that the nitrile catholyte performs better at higher voltages and higher state of charge than do carbonate catholytes, when assembled with a solid-state electrolyte as in this Example.
Example 2—Stability Tests of Electrochemical Cells Having Nitrile or Carbonate Cathode Electrolytes
This Example compares electrolyte performance when the coin cell cap, on the anode side, has been compromised. In this example, a hole was drilled into the coin cell cap, on the anode side. The cell included a cathode, layered with a electrolyte (i.e., catholyte), which was layered with a solid garnet separator, and to which the opposite side of the solid garnet separator was layered with Li metal by evaporation. The cell was maintained at a pressure of about 50-300 psi. The electrolyte included ethylene carbonate:ethyl-methyl-carbonate (EC:EMC) in a 3:7 w/w ratio+1M LiPF6 at 2 w/w FEC.
In a second cell, the cell included a cathode, layered with a electrolyte (i.e., catholyte),which was layered with a solid garnet separator, and to which the opposite side of the solid garnet separator was layered with Li metal by evaporation. The cell was maintained at a pressure of about 50-300 psi. The electrolyte included succinonitrile and 12 mol % LiBF4.
Both of the two cell batches in this Example were tested in a glovebox at 45° C. within an hour of the crimping. 1/16 inch holes were pre-drilled in the anode cap, which was then used in a standard cell build. Within an hour after crimping, the cells were put on test in a argon-filled glove box at 45° C. The test included a GITT charge-discharge protocol of a pulsed C/10 charge followed by a pulsed C/3 discharge.
The results are presented in FIG. 4. The cell with the nitrile electrolyte maintained a substantial fraction of its capability to discharge energy, while the cell with the carbonate electrolyte did not maintain a substantial fraction of its capability to discharge energy.
Example 3—Stability Tests of Electrochemical Cells Having Nitrile or Carbonate Cathode Electrolytes
This Example compares the storage stability of two types of electrochemical cells. One electrochemical cell included a cathode, layered with a gel electrolyte (i.e., catholyte), which was layered with a solid garnet separator, and to which the opposite side of the solid garnet separator was layered with Li metal by evaporation. The cell was maintained at a pressure of about 50-300 psi. The cell included a seal around the garnet to isolate the cathode/catholyte from the lithium anode. The gel electrolyte included ethylene carbonate:ethyl-methyl-carbonate (EC:EMC) in a 3:7 w/w ratio+1M LiPF6 at 2 w/w FEC.
A second electrochemical cell included a cathode, layered with a electrolyte (i.e., catholyte),which was layered with a solid garnet separator, and to which the opposite side of the solid garnet separator was layered with Li metal by evaporation. The cell was maintained at a pressure of about 50-300 psi. The electrolyte included succinonitrile and 12 mol % LiBF4.
Both of the two cells were monitored for impedance growth during cycling. The electrochemical cell having the succinonitrile solvent in the cathode electrolyte was observed to have a lower impedance growth, over 50 cycles, when compared to the electrochemical cell having the carbonate solvent in the cathode electrolyte. The electrochemical cell having the succinonitrile solvent therefore had a greater power and energy capability than the electrochemical cell having the carbonate solvent in the cathode electrolyte.
The results are presented in FIG. 5.
Example 4—Stability Tests of Electrochemical Cells Having Nitrile or Carbonate Cathode Electrolytes
In this example, two PVDF-HFP gel polymer films were soaked in adiponitrile or EC:EMC. While the gel films were held at 45° C., the films were monitored for mass loss over time in an open system. Over two hours, the EC:EMC evaporated quickly and significantly, whereas the adiponitrile was stable and did not evaporate quickly or significantly. This shows that the nitrile catholyte is more stable within the cathode at elevated temperature than is the carbonate catholyte. The nitrile catholyte should therefore be suitable for use in high temperature operations.
The results are shown in FIG. 6 and Table 1, below:
TABLE 1
EC:EMC (3:7 vol %) + Adiponitrile + 1M
1M LiPF6 LiTFSI
% solvent loss on drying 57 1
This data shows that the solvent loss on drying is much lower for nitrile solvents than for carbonate solvents.
Catholyte volatility is problematic for safety and physical stability reasons. The Example herein shows that the selected dinitriles are much less prone to solvent evaporation as compared to carbonates.
Example 5—Stability Tests of Electrochemical Cells Having Sulfolane Cathode Electrolytes
Using the Micromeritics BET tool, open beakers were prepared with the following compostions in Table 2 at 45° C. with the compositions shown in the Table 2, and the vapor pressure was noted. Over two hours, the EC:EMC evaporated quickly and significantly, whereas the sulfolane system was stable and did not evaporate quickly or significantly. This shows that the sulfur-including catholyte is more physically stable within the cathode at elevated temperature than is the carbonate or nitrile catholyte. The sulfur-including catholyte should therefore be suitable for use in high temperature operations.
TABLE 2
LOW VAPOR PRESSURE (MEASURED VALUE)
Vapor Pressure at 45° C.
Composition (mmHg)
Ethylene Carbonate + 0.23
Sulfolane 3:7 v/v
Glutaronitrile + 0.68
Succinonitrile 0.57:0.43 mol/mol
EC:EMC 3:7 w/w 27.2
Example 6—High Voltage Storage at a Minimal Capacity Loss
Full cells were prepared with two different catholytes: in one case, ethylene carbonate with 2M LiPF6, and in the second case, sulfolane with 2M LiPF6. Each full cell device was stored at 45° C. after charging to 4.5V. Each week the device was discharged, and the measured discharge capacity that remained after the week of high temperature storage is called the self-discharged capacity. Then the device was charged and discharged, and the difference between the original capacity and the newly measured reversible capacity provided the irreversible capacity loss after high voltage storage. The device was charged to 4.5V and stored for another week before repeating the discharge tests. The cells retained both self-discharged capacity and reversible capacity for four weeks of storage at 4.5V.
In this example, cathode is prepared with mass fraction 0.91 NMC, 0.010 Ketjenblack EC-600JD, 0.050 Kynar Powerflex LBG PVDF 12C9073, 0.030 SuperC65; mixed with NMP (N-mthyl-2-pyrolidone) and degassed, then cast on carbon-coated aluminum foil, dried at 120° C. under vacuum, and calendered. There was no bonding layer. Separator was 120 μm thick.
Example 7—ASR Growth for a Sulfolane System
As shown in FIG. 7, ASR growth wherein the cell was prepared with sulfolane and ethylene carbonate (3:7 v/v)+2M LiPF6 was a lot smaller than a cell prepared with ethyl-methyl carbonate, ethylene carbonate (3:7 v/v)+1M LiPF6. The data was obtained for 10 cycles, C/3 pulses, from 2.7-4.2 V at 45° C. The cathode was NMC, and the separator was solid-state separator material. As shown in FIG. 8, a cell was able to charge and discharge energy for 500 cycles with minimal gain in ASR.
As shown in these Examples, the electrochemical performance for electrochemical cells having a nitrile catholyte is surprisingly improved when compared to electrochemical cells having a carbonate catholyte. As shown in these Examples, high temperature physical stability, high voltage stability, elevated temperature power capability, and cycle life are much better for electrochemical cells having a nitrile catholyte than they are for electrochemical cells having a carbonate catholyte.
The embodiments and examples described above are intended to be merely illustrative and non-limiting. Those skilled in the art will recognize or will be able to ascertain using no more than routine experimentation, numerous equivalents of specific compounds, materials and procedures. All such equivalents are considered to be within the scope and are encompassed by the appended claims.

Claims (21)

What is claimed is:
1. An electrochemical cell, comprising:
a lithium metal negative electrode;
a solid separator in direct contact with the lithium metal negative electrode, wherein the solid separator is a thin film and has a film thickness of about 10 nm to about 100 μm; and
a positive electrode,
wherein the positive electrode comprises:
an active material; and
a catholyte,
wherein the catholyte comprises:
a catholyte solvent; and
a lithium salt; and
wherein the catholyte solvent comprises:
(a) a nitrile solvent, a dinitrile solvent, an organic sulfur-including solvent, or combinations thereof; and
(b) a member selected from the group consisting of methylene methanedisulfonate (MMDS), methyl pivalate, 1,2 dioxane, sulfolane, and combinations thereof.
2. The electrochemical cell of claim 1, wherein the catholyte solvent comprises a solvent selected from the group consisting of a nitrile solvent, a dinitrile solvent, and a combination thereof.
3. The electrochemical cell of claim 1, wherein the lithium metal negative electrode is a layer laminated to the solid separator; and wherein the solid separator is a layer laminated to the positive electrode.
4. The electrochemical cell of claim 1, wherein the solid separator is impermeable to the catholyte.
5. The electrochemical cell of claim 1, further comprising a bonding layer between the positive electrode and the solid separator.
6. The electrochemical cell of claim 5, wherein the bonding layer comprises a solvent and a lithium salt;
wherein the solvent in the bonding layer is selected from the group consisting of ethylene carbonate, methylene carbonate, methyl ethyl carbonate, and diethylene carbonate;
wherein the lithium salt is selected from LiPF6, LiBOB, LiBETI, LiTFSi, LiBF4, LiClO4, LiAsF6, LiFSI, LiI, and a combination thereof.
7. The electrochemical cell of claim 6, wherein the bonding layer further comprises a polymer selected from the group consisting of polyacrylonitrile (PAN), polyethylene, polypropylene, polyethylene oxide (PEO), polymethyl methacrylate (PMMA), polyvinyl chloride (PVC), polyvinyl pyrrolidone (PVP), polyethylene oxide poly(allyl glycidyl ether) PEO-AGE, polyethylene oxide 2-(methoxyethoxy)ethyl glycidyl ether (PEO-MEEGE), polyethylene oxide 2-(methoxyethoxy)ethyl glycidyl poly(allyl glycidyl ether) (PEO-MEEGE-AGE), polysiloxane, polyvinylidene fluoride (PVdF), polyvinylidene fluoride hexafluoropropylene (PVdF-HFP), rubbers, nitrile rubber (NPR), styrene-butadiene-rubber (SBR), polybutadiene polymer, polybutadiene rubber (PB), polyisobutadiene rubber (PIB), polyisoprene rubber (PI), polychloroprene rubber (CR), acrylonitrile-butadiene rubber (NBR), polyethyl acrylate (PEA), and combinations thereof.
8. The electrochemical cell of claim 5, wherein the solvent in the bonding layer is selected from ethylene carbonate (EC), diethylene carbonate, diethyl carbonate, dimethyl carbonate (DMC), ethyl-methyl carbonate (EMC), tetrahydrofuran (THF), γ-Butyrolactone (GBL), fluoroethylene carbonate (FEC), fluoromethyl ethylene carbonate (FMEC), trifluoroethyl methyl carbonate (F-EMC), fluorinated 3-(1,1,2,2-tetrafluoroethoxy)-1,1,2,2-tetrafluoropropane (i.e., 1,1,2,2-Tetrafluoro-3-(1,1,2,2-tetrafluoroethoxy)propane, F-EPE), fluorinated cyclic carbonate (F-AEC), propylene carbonate (PC), dioxolane, acetonitrile (ACN), succinonitrile, adiponitrile, hexanedinitrile, a mixture of adiponitrile and hexanedinitrile, pentanedinitrile, acetophenone, isophorone, benzonitrile, dimethyl sulfate, dimethyl sulfoxide (DMSO), ethyl acetate, methyl butyrate, dimethyl ether (DME), diethyl ether, propylene carbonate, dioxolane, glutaronitrile, and combinations thereof.
9. The electrochemical cell of claim 5, wherein the solvent in the bonding layer is a 1:1 w/w mixture of EC:PC.
10. The electrochemical cell of claim 5, wherein the lithium salt in the bonding layer is selected from LiPF6, LiBOB, LiFTSi, and combinations thereof.
11. The electrochemical cell of claim 1, wherein the solid separator is selected from a lithium sulfide, a lithium borohydride, a LiPON, a lithium-stuffed garnet, a lithium-rich antiperovskite, a LISICON, and a combination thereof.
12. The electrochemical cell of claim 11, wherein the solid separator is an oxide selected from a lithium-stuffed garnet characterized by the formula LixLay-ZrzOt.qAl2O3, wherein 4<x<10, 1<y<4, 1<z<3, 6<t<14, 0≤q≤1.
13. The electrochemical cell of claim 1, wherein the catholyte solvent is a solvent having a HOMO level of more than 7.2 eV below the vacuum level and up to 11.5 eV below the vacuum level.
14. The electrochemical cell of claim 1, wherein the catholyte solvent comprises a solvent selected from acetonitrile, methoxyacetonitrile, butyronitrile, benzonitrile, hexanenitrile, fluoroacetonitrile, nitroacetonitrile, ethoxyacetonitrile, pentanenitrile, propanenitrile, malononitrile, iso-butyronitrile, and combinations thereof.
15. The electrochemical cell of claim 1, wherein the catholyte further comprises a solvent selected from ethylene carbonate (EC), diethylene carbonate, diethyl carbonate, dimethyl carbonate (DMC), ethyl-methyl carbonate (EMC), tetrahydrofuran (THF), γ-Butyrolactone (GBL), fluoroethylene carbonate (FEC), fluoromethyl ethylene carbonate (FMEC), trifluoroethyl methyl carbonate (F-EMC), fluorinated 3-(1,1,2,2-tetrafluoroethoxy)-1,1,2,2-tetrafluoropropane (i.e., 1,1,2,2-tetrafluoro-3-(1,1,2,2-tetrafluoroethoxy)propane (F-EPE)), fluorinated cyclic carbonate (F-AEC), propylene carbonate (PC), dioxolane, acetonitrile (ACN), succinonitrile, adiponitrile, hexanedinitrile, pentanedinitrile, acetophenone, isophorone, benzonitrile, dimethyl sulfate, dimethyl sulfoxide (DMSO), ethyl acetate, methyl butyrate, dimethyl ether (DME), diethyl ether, dioxolane, glutaronitrile, and combinations thereof.
16. The electrochemical cell of claim 1, wherein the catholyte solvent has a stability window up to 4.7 V v. Lithium.
17. The electrochemical cell of claim 1, wherein the catholyte solvent comprises a nitrile represented by Formula (I):
Figure US11342630-20220524-C00008
wherein:
R1, R2, R3, and R4 are, independently in each instance, selected from —CN, —NO2, —CO2, —SO4, —SO3, —SO2, —CH2—SO3, —CHF—SO3, —CF2—SO3, —H, —F, —Cl, —Br, and —I; and
wherein subscript m is an integer from 1 to 1000.
18. The electrochemical cell of claim 1, wherein the catholyte solvent comprises a nitrile is selected from the following nitriles:
Figure US11342630-20220524-C00009
and combinations thereof.
19. The electrochemical cell of claim 1, wherein the solid separator comprises:
a lithium-stuffed garnet oxide characterized by the formula LiuLavZrxOy.zAl2O3, wherein
u is a rational number from 4 to 8;
v is a rational number from 2 to 4;
x is a rational number from 1 to 3;
y is a rational number from 10 to 14; and
z is a rational number from 0.05 to 1;
wherein u, v, x, y, and z are selected so that the lithium-stuffed garnet oxide is charge neutral.
20. The electrochemical cell of claim 7, wherein the polyethylene is low density linear polyethylene.
21. The electrochemical cell of claim 7, wherein the rubbers are ethylene propylene (EPR).
US16/326,852 2016-08-29 2017-08-29 Catholytes for solid state rechargeable batteries, battery architectures suitable for use with these catholytes, and methods of making and using the same Active 2038-02-23 US11342630B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US16/326,852 US11342630B2 (en) 2016-08-29 2017-08-29 Catholytes for solid state rechargeable batteries, battery architectures suitable for use with these catholytes, and methods of making and using the same

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US201662380942P 2016-08-29 2016-08-29
PCT/US2017/049218 WO2018044952A1 (en) 2016-08-29 2017-08-29 Catholytes for solid state rechargeable batteries, battery architectures suitable for use with these catholytes, and methods of making and using the same
US16/326,852 US11342630B2 (en) 2016-08-29 2017-08-29 Catholytes for solid state rechargeable batteries, battery architectures suitable for use with these catholytes, and methods of making and using the same

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2017/049218 A-371-Of-International WO2018044952A1 (en) 2016-08-29 2017-08-29 Catholytes for solid state rechargeable batteries, battery architectures suitable for use with these catholytes, and methods of making and using the same

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US17/726,440 Continuation US12057600B2 (en) 2016-08-29 2022-04-21 Catholytes for solid state rechargeable batteries, battery architectures suitable for use with these catholytes, and methods of making and using the same

Publications (2)

Publication Number Publication Date
US20190198838A1 US20190198838A1 (en) 2019-06-27
US11342630B2 true US11342630B2 (en) 2022-05-24

Family

ID=61301484

Family Applications (2)

Application Number Title Priority Date Filing Date
US16/326,852 Active 2038-02-23 US11342630B2 (en) 2016-08-29 2017-08-29 Catholytes for solid state rechargeable batteries, battery architectures suitable for use with these catholytes, and methods of making and using the same
US17/726,440 Active US12057600B2 (en) 2016-08-29 2022-04-21 Catholytes for solid state rechargeable batteries, battery architectures suitable for use with these catholytes, and methods of making and using the same

Family Applications After (1)

Application Number Title Priority Date Filing Date
US17/726,440 Active US12057600B2 (en) 2016-08-29 2022-04-21 Catholytes for solid state rechargeable batteries, battery architectures suitable for use with these catholytes, and methods of making and using the same

Country Status (3)

Country Link
US (2) US11342630B2 (en)
EP (1) EP3504749A4 (en)
WO (1) WO2018044952A1 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11962002B2 (en) 2021-12-17 2024-04-16 Quantumscape Battery, Inc. Cathode materials having oxide surface species
US11967676B2 (en) 2021-11-30 2024-04-23 Quantumscape Battery, Inc. Catholytes for a solid-state battery
US12074276B2 (en) 2018-11-06 2024-08-27 Quantumscape Battery, Inc. Electrochemical cells with catholyte additives and lithium-stuffed garnet separators

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6668231B2 (en) 2013-05-15 2020-03-18 クアンタムスケイプ コーポレイション Solid catholyte or electrolyte for batteries
EP3314681B1 (en) 2015-06-24 2021-07-21 QuantumScape Battery, Inc. Composite electrolytes
EP3384548A4 (en) 2015-12-04 2019-07-24 QuantumScape Corporation COMPOSITIONS OF ELECTROLYTES AND CATHOLYTES COMPRISING LITHIUM, PHOSPHORUS, SULFUR AND IODINE, ELECTROLYTE MEMBRANES FOR ELECTROCHEMICAL DEVICES, AND ANNEALING METHODS FOR THE PRODUCTION OF THESE ELECTROLYTES AND CATHOLYTES
CN113555604A (en) * 2018-04-11 2021-10-26 宁德新能源科技有限公司 Lithium Ion Battery
CN109256525B (en) * 2018-08-28 2021-07-27 长沙矿冶研究院有限责任公司 High-density flexible electrode plate for all-solid-state battery and preparation method thereof
CN110970621B (en) * 2018-09-30 2021-02-26 宁德时代新能源科技股份有限公司 Lithium ion battery
KR20220117314A (en) * 2019-12-20 2022-08-23 유미코아 Electrolyte for Lithium Secondary Batteries
EP4195311A4 (en) * 2020-09-21 2024-10-30 LG Energy Solution, Ltd. LITHIUM SECONDARY BATTERY AND METHOD FOR MANUFACTURING THE SAME
CN112186260A (en) * 2020-09-28 2021-01-05 苏州酷卡环保科技有限公司 Formation method of lithium ion battery
EP4264734A4 (en) * 2020-12-15 2025-07-09 Ses Holdings Pte Ltd RECHARGEABLE BATTERY
CN113782831A (en) * 2021-08-03 2021-12-10 华中科技大学 High-voltage-resistant lithium ion battery electrolyte and preparation method and application thereof
CN114976245A (en) * 2022-06-16 2022-08-30 张家港市国泰华荣化工新材料有限公司 Non-aqueous electrolyte and lithium battery
CN116217355A (en) * 2023-05-08 2023-06-06 宁德时代新能源科技股份有限公司 The preparation method of fluorinated acetal compound
CN119340491B (en) * 2023-07-18 2025-11-04 宁德时代新能源科技股份有限公司 Lithium secondary batteries and electrical devices
CN118352479B (en) * 2024-06-18 2024-09-13 浙江省白马湖实验室有限公司 Preparation method of self-supporting lithium ion sulfur battery positive electrode

Citations (127)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4183988A (en) 1978-11-16 1980-01-15 General Electric Company Solid ion-conductive electrolyte
JPS57108831A (en) 1980-12-26 1982-07-07 Hitachi Maxell Ltd Manufacture of solid electrolytic thin plate
US4357401A (en) 1980-03-31 1982-11-02 L'etat Francais Represente Par Le Delegue General Pour L'armement Macromolecular material of ionic conduction
US4654279A (en) 1986-07-10 1987-03-31 The United States Of America As Represented By The Secretary Of The Navy Interpenetrating-network polymeric electrolytes
US4668736A (en) 1984-07-18 1987-05-26 Minnesota Mining And Manufacturing Company Fast curing epoxy resin compositions
US4868262A (en) 1987-07-15 1989-09-19 Th. Goldschmidt Ag Copolymers with epoxide groups, their synthesis and use for finishing textile fibers or fiber products
US4990413A (en) 1989-01-18 1991-02-05 Mhb Joint Venture Composite solid electrolytes and electrochemical devices employing the same
US4990587A (en) 1987-06-26 1991-02-05 The Secretary Of State For Defence In Her Britannic Majesty's Government Of The United Kingdom And Northern Ireland Method of preparing toughened epoxy polymers
US5202009A (en) 1989-10-26 1993-04-13 Compagnie Generale D'electricite Electrolyte solid polymer reticule
US5449576A (en) 1993-11-26 1995-09-12 Motorola, Inc. Multilayered electrolyte and electrochemical cells using same
DE19825807A1 (en) 1997-06-10 1998-12-24 Samsung Display Devices Co Ltd A glass-polymer composite electrolyte and a method for producing the same
EP0977296A1 (en) 1997-09-03 2000-02-02 Matsushita Electric Industrial Co., Ltd. Solid electrolytic moldings, electrode moldings, and electrochemical elements
US6030720A (en) 1994-11-23 2000-02-29 Polyplus Battery Co., Inc. Liquid electrolyte lithium-sulfur batteries
US6210836B1 (en) 1998-04-14 2001-04-03 Matsushita Electric Industrial Co., Ltd. Lithium secondary battery
US6277524B1 (en) 1997-12-09 2001-08-21 Toyota Jidosha Kabushiki Kaisha Lithium-ion-conductive solid electrolyte and solid-electrolyte lithium battery
JP2001316583A (en) 2000-05-02 2001-11-16 Tsutomu Minami Lithium-ion conductive organic-inorganic composite
US6365300B1 (en) 1998-12-03 2002-04-02 Sumitomo Electric Industries, Ltd. Lithium secondary battery
US20030031931A1 (en) 2001-08-07 2003-02-13 3M Innovative Properties Company Lithium-ion batteries
JP2003217663A (en) 2002-01-16 2003-07-31 Japan Storage Battery Co Ltd Non-aqueous electrolyte battery
US20030157409A1 (en) 2002-02-21 2003-08-21 Sui-Yang Huang Polymer lithium battery with ionic electrolyte
US20030198870A1 (en) 2002-02-27 2003-10-23 Fuji Photo Film Co., Ltd. Electrolytic composition and non-aqueous electrolytic secondary battery
US6656641B1 (en) 1997-08-21 2003-12-02 University Of Dayton Methods of enhancing conductivity of a polymer-ceramic composite electrolyte
US20040096747A1 (en) 2001-01-30 2004-05-20 Andree Schwake Electrolyte solution for electrochemical cells
US20050026037A1 (en) 2002-07-26 2005-02-03 A123 Systems, Inc. Bipolar articles and related methods
US20060068296A1 (en) 2002-11-29 2006-03-30 Hiroe Nakagawa Nonaqueous electrolyte and nonaqueous-electrolyte battery
US20060166003A1 (en) 2003-06-16 2006-07-27 William Marsh Rice University Fabrication of carbon nanotube reinforced epoxy polymer composites using functionalized carbon nanotubes
US20060216603A1 (en) 2005-03-26 2006-09-28 Enable Ipc Lithium-ion rechargeable battery based on nanostructures
US20060246355A1 (en) 2005-04-27 2006-11-02 Samsung Sdi Co., Ltd. Lithium secondary battery
US20070015022A1 (en) 2005-07-12 2007-01-18 Samsung Sdi Co., Ltd. Ion conductive composite membrane using inorganic conductor and method of manufacturing the same
CN1925203A (en) 2005-08-31 2007-03-07 株式会社小原 Lithium ion secondary battery and solid electrolyte therefor
CN1949569A (en) 2005-10-13 2007-04-18 株式会社小原 Lithium ion conductive solid electrolyte and method for manufacturing the same
US20070117026A1 (en) 2005-11-21 2007-05-24 Binod Kumar Solid composite electrolyte membrane and method of making
US20070117007A1 (en) 2005-11-23 2007-05-24 Polyplus Battery Company Li/air non-aqueous batteries
US20070160911A1 (en) 2004-02-12 2007-07-12 Masahiro Tatsumisago Lithium ion conducting sulfide based crystallized glass and method for production thereof
US20070172739A1 (en) 2005-12-19 2007-07-26 Polyplus Battery Company Composite solid electrolyte for protection of active metal anodes
CN101013761A (en) 2007-02-13 2007-08-08 中国科学院上海硅酸盐研究所 Solid electrolyte material system for all solid state lithium battery and preparation method
US20070231704A1 (en) 2006-03-30 2007-10-04 Ohara Inc. Lithium ion conductive solid electrolyte and production process thereof
JP2007273214A (en) 2006-03-31 2007-10-18 Idemitsu Kosan Co Ltd Solid electrolyte, method for producing the same, and all-solid-state secondary battery
JP2007273217A (en) 2006-03-31 2007-10-18 Idemitsu Kosan Co Ltd Solid electrolyte, method for producing the same, and all-solid-state secondary battery
CN101174698A (en) 2006-10-31 2008-05-07 株式会社小原 Lithium ion conductive solid electrolyte and a method for manufacturing the same
US20080131781A1 (en) 2004-08-17 2008-06-05 Lg Chem, Ltd. Lithium Secondary Batteries With Enhanced Safety And Performance
US20080200589A1 (en) 2005-07-15 2008-08-21 Huntsman International Llc Toughened Composition
US7416815B2 (en) 2004-04-01 2008-08-26 Sumitomo Electric Industries, Ltd. Negative electrode member for lithium battery and process for producing the same
US20090087751A1 (en) 2007-09-05 2009-04-02 Seiko Epson Corporation Solid electrolyte material of conducting lithium ion, battery device using the solid electrolyte material and all-solid lithium secondary battery provided with the battery device
US20090136830A1 (en) 2007-11-27 2009-05-28 John Howard Gordon Substantially Solid, Flexible Electrolyte For Alkili-Metal-Ion Batteries
US20090182066A1 (en) 2007-12-27 2009-07-16 E. I. Du Pont De Nemours And Company Crosslinkable fluoropolymer, crosslinked fluoropolymers and crosslinked fluoropolymer membranes
JP2009176541A (en) 2008-01-23 2009-08-06 Idemitsu Kosan Co Ltd Solid electrolyte membrane, positive electrode membrane, or negative electrode membrane for all solid lithium secondary battery, method for producing the same, and all solid lithium secondary battery
US20090208806A1 (en) 2005-02-15 2009-08-20 Toray Industries, Inc. Method for producing polymer electrolyte molded article, polymer electrolyte material, polymer electrolyte membrane, and polymer electrolyte fuel cell
US20090226816A1 (en) 2006-11-14 2009-09-10 Ngk Insulators, Ltd. Solid electrolyte structure for all-solid-state battery, all-solid-state battery, and their production methods
CN101542777A (en) 2007-02-05 2009-09-23 Lg化学株式会社 Organic/inorganic composite separator having porous active coating layer and electrochemical device comprising the same
US20100019194A1 (en) 2006-12-26 2010-01-28 Tetsu Fujiwara Positive electrode active material for nonaqueous electrolyte secondary battery, positive electrode and secondary battery
US20100028768A1 (en) 2007-08-02 2010-02-04 Sony Corporation Positive electrode active material, positive electrode using the same and non-aqueous electrolyte secondary battery
US20100151335A1 (en) 2005-08-02 2010-06-17 Idemitsu Kosan Co., Ltd. Solid electrolyte sheet
US20100183924A1 (en) 2009-01-22 2010-07-22 Hanwha Chemical Corporation Electrode-active anion-deficient non-stoichiometric lithium iron phosphate, method for preparing the same, and electrochemical device using the same
JP2011044249A (en) 2009-08-19 2011-03-03 Toyota Motor Corp Sulfide solid electrolyte material
US7901598B2 (en) 2006-05-15 2011-03-08 Sumitomo Electric Industries, Ltd. Solid electrolyte and method of producing the same
US7915378B2 (en) 2002-04-26 2011-03-29 Hideyuki Nishio Material for solid polymer electrolyte, and polyether polymer and process for producing same
US20110076570A1 (en) 2009-09-29 2011-03-31 Toyota Jidosha Kabushiki Kaisha Solid state electrolyte layer, electrode active material layer, all solid state lithium battery, manufacturing method for solid state electrolyte layer, and manufacturing method for electrode active material layer
CN102106030A (en) 2008-07-23 2011-06-22 丰田自动车株式会社 Polymer electrolyte membrane, method for producing polymer electrolyte membrane, and solid polymer fuel cell
US20110229765A1 (en) 2003-04-03 2011-09-22 Jeremy Barker Electrodes Comprising Mixed Active Particles
US20110262816A1 (en) 2009-01-12 2011-10-27 Glenn Amatucci Polyhydrogen fluoride based battery
US20110259505A1 (en) 2009-09-29 2011-10-27 Lg Chem, Ltd. Method for manufacturing separator, separator manufactured therefrom and method for manufacturing electrochemical device having the same
US20110311875A1 (en) 2008-11-20 2011-12-22 Lg Chem, Ltd. Electrode active material for secondary battery and method for preparing the same
JP2012054212A (en) 2010-09-03 2012-03-15 Toyota Motor Corp Sulfide solid electrolyte material, method for producing sulfide solid electrolyte material, and lithium solid battery
US20120094185A1 (en) 2009-05-01 2012-04-19 Toyota Jidosha Kabushiki Kaisha Solid electrolyte material, electrode element that includes solid electrolyte material, all-solid battery that includes solid electrolyte material, and manufacturing method for solid electrolyte material
US20120115763A1 (en) 2009-12-30 2012-05-10 Exxonmobil Research And Engineering Company Lubricant compositions based on block copolymers and processes for makin
JP2012146512A (en) 2011-01-12 2012-08-02 Toyota Motor Corp Method for manufacturing battery
US20120196186A1 (en) 2008-06-20 2012-08-02 Toyota Motor Engineering & Manufacturing North America, Inc. Electrode material with core-shell structure
US20120208062A1 (en) 2008-12-26 2012-08-16 Haoshen Zhou Lithium secondary cell
US20120244411A1 (en) 2009-10-02 2012-09-27 Sumitomo Chemical Company, Limited Lithium-containing metal oxide, and non-aqueous electrolyte secondary battery
US20120276459A1 (en) 2011-04-29 2012-11-01 National University Corporation Mie University Negative electrode for lithium secondary battery, method of manufacturing the same, and lithium secondary battery employing the same
WO2012156795A1 (en) 2011-05-18 2012-11-22 Toyota Jidosha Kabushiki Kaisha Method of producing solid sulfide electrolyte material and solid sulfide electrolyte material
US20130004843A1 (en) 2011-06-29 2013-01-03 Hitachi, Ltd. Electrode for lithium ion battery, manufacturing method thereof, lithium ion battery, and manufacturing method thereof
JP2013012416A (en) 2011-06-29 2013-01-17 Sumitomo Electric Ind Ltd Nonaqueous electrolyte battery and nonaqueous electrolyte battery manufacturing method
US20130040208A1 (en) 2010-03-26 2013-02-14 Toyota Jidosha Kabushiki Kaisha Sulfide solid electrolyte material, battery, and method for producing sulfide solid electrolyte material
US20130052509A1 (en) 2011-08-25 2013-02-28 GM Global Technology Operations LLC Lithium ion battery with electrolyte-embedded separator particles
JP2013045683A (en) 2011-08-25 2013-03-04 Sumitomo Electric Ind Ltd Electrode for solid electrolyte battery, solid electrolyte layer, solid electrolyte battery, and binder used for the same
US20130095358A1 (en) 2011-10-13 2013-04-18 Eveready Battery Company, Inc. Lithium Iron Disulfide Battery
US20130108934A1 (en) 2011-10-27 2013-05-02 National University Corporation Mie University Electrolyte for lithium air battery and lithium air battery including the same
JP2013080616A (en) 2011-10-04 2013-05-02 Seiko Epson Corp Lithium ion secondary battery and method of manufacturing wound body
US20130216910A1 (en) 2010-11-09 2013-08-22 3M Innovative Properties Company High capacity alloy anodes and lithium-ion electrochemical cells containing same
WO2013125485A1 (en) 2012-02-24 2013-08-29 住友電気工業株式会社 All-solid-state lithium secondary battery
US8524393B2 (en) 2009-11-25 2013-09-03 Toyota Jidosha Kabushiki Kaisha Method for producing electrode laminate and electrode laminate
US20130230778A1 (en) 2012-03-02 2013-09-05 Honda Motor Co., Ltd. Lithium ion conductive composite electrolyte and lithium ion secondary battery using same
US20140023940A1 (en) 2010-12-01 2014-01-23 Hydro-Quebec Lithium-air battery
JP2014038755A (en) 2012-08-14 2014-02-27 Toyota Motor Corp Manufacturing method of sulfide solid electrolytic material
US20140065513A1 (en) 2012-08-29 2014-03-06 Michael Edward Badding Ion-conducting composite electrolyte comprising path-engineered particles
US20140072866A1 (en) * 2012-09-12 2014-03-13 Sony Corporation Secondary battery, battery pack, and electric vehicle
WO2014073197A1 (en) 2012-11-06 2014-05-15 出光興産株式会社 Solid electrolyte
US8729866B2 (en) 2009-09-02 2014-05-20 Toyota Jidosha Kabushiki Kaisha Sulfide-based all-solid-state lithium secondary battery system
US20140141341A1 (en) 2011-07-06 2014-05-22 Toyota Jidosha Kabushiki Kaisha Sulfide solid electrolyte material, lithium solid-state battery, and method for producing sulfide solid electrolyte material
US20140170504A1 (en) 2012-12-14 2014-06-19 Samsung Electronics Co., Ltd. Flexible solid electrolyte, all-solid-state lithium battery including the flexible solid electrolyte, and method of preparing the flexible solid electrolyte
US20140170465A1 (en) * 2004-02-06 2014-06-19 Polyplus Battery Company Protected lithium electrodes having a porous electrolyte interlayer and associated battery cells
US20140193695A1 (en) 2012-03-13 2014-07-10 Kabushiki Kaisha Toshiba Lithium-ion conducting oxide, solid electrolyte secondary battery and battery pack
US20140193693A1 (en) 2012-03-16 2014-07-10 Kabushiki Kaisha Toshiba Lithium-ion conductive sulfide, solid electrolyte secondary battery and battery pack
US20140197800A1 (en) 2011-07-26 2014-07-17 Toyota Jidosha Kabushiki Kaisha Lithium solid state secondary battery system
KR20140095658A (en) 2013-01-24 2014-08-04 엘지전자 주식회사 Solar cell
CN104011926A (en) 2011-11-02 2014-08-27 I-Ten公司 Method for preparing solid electrolyte film for lithium ion battery
US8871391B2 (en) 2012-05-03 2014-10-28 Ut-Battelle, Llc Lithium sulfide compositions for battery electrolyte and battery electrode coatings
CN104143656A (en) 2014-07-04 2014-11-12 中南大学 A kind of preparation method of inorganic solid electrolyte membrane/electrode composite material
CN104159869A (en) 2012-03-02 2014-11-19 日本碍子株式会社 Solid electrolyte ceramic material and production method therefor
WO2014186634A2 (en) 2013-05-15 2014-11-20 Quantumscape Corporation Solid state catholyte or electrolyte for battery using liampbsc (m = si, ge, and/or sn)
US20140363745A1 (en) 2011-12-22 2014-12-11 Toyota Jidosha Kabushiki Kaisha Sulfide solid electrolyte material, battery, and producing method for sulfide solid electrolyte material
JP2014241240A (en) 2013-06-12 2014-12-25 トヨタ自動車株式会社 Method for manufacturing sulfide all-solid battery
US20150017548A1 (en) 2012-02-06 2015-01-15 Toyota Jidosha Kabushiki Kaisha Sulfide solid electrolyte material, battery, and producing method for sulfide solid electrolyte material
US20150037687A1 (en) 2012-02-06 2015-02-05 Tokyo Institute Of Technology Sulfide solid electrolyte material, battery, and producing method for sulfide solid electrolyte material
CN104377385A (en) 2014-09-26 2015-02-25 珠海光宇电池有限公司 Lithium ion secondary battery composite electrolyte film, and making method and application thereof
US20150056496A1 (en) 2013-08-23 2015-02-26 Ut-Battelle, Llc Lithium-conducting sulfur compound cathode for lithium-sulfur batteries
JP2015050072A (en) 2013-09-02 2015-03-16 日本碍子株式会社 Solid electrolyte ceramic materials
US20150085423A1 (en) 2012-04-18 2015-03-26 The Arizona Board Of Regents, A Body Corporate Act For And On Behalf Of Structural Supercapacitors
US20150099190A1 (en) * 2013-10-07 2015-04-09 Quantumscape Corporation Garnet materials for li secondary batteries and methods of making and using garnet materials
CN104538670A (en) 2014-11-24 2015-04-22 深圳华中科技大学研究院 All-solid polymer electrolyte, and preparation method and application of all-solid polymer electrolyte
US20150111110A1 (en) 2012-04-27 2015-04-23 Kabushiki Kaisha Toyota Jidoshokki Solid electrolyte and secondary battery
US20150118574A1 (en) 2013-10-31 2015-04-30 Samsung Electronics Co., Ltd. Positive electrode for lithium-ion secondary battery, and lithium-ion secondary battery
US20150171463A1 (en) 2013-12-12 2015-06-18 Ut-Battelle, Llc High conducting oxide - sulfide composite lithium superionic conductor
US20150287986A1 (en) 2006-03-22 2015-10-08 Sion Power Corporation Electrode protection in both aqueous and non-aqueous electrochemical cells, including rechargeable lithium batteries
US9172112B2 (en) 2010-08-05 2015-10-27 Toyota Jidosha Kabushiki Kaisha Sulfide solid electrolyte glass, lithium solid state battery and producing method of sulfide solid electrolyte glass
US9252455B1 (en) * 2010-04-14 2016-02-02 Hrl Laboratories, Llc Lithium battery structures employing composite layers, and fabrication methods to produce composite layers
EP2983231A1 (en) 2013-04-02 2016-02-10 Idemitsu Kosan Co., Ltd. Composite material
US20160156065A1 (en) 2014-12-02 2016-06-02 Polyplus Battery Company Standalone sulfide based lithium ion-conducting glass solid electrolyte and associated structures, cells and methods
US20160164136A1 (en) 2013-07-04 2016-06-09 Mitsui Mining & Smelting Co., Ltd. Crystalline solid electrolyte and production method therefor
US20160181585A1 (en) 2014-12-19 2016-06-23 Samsung Electronics Co., Ltd. Composite membrane, preparation method thereof, anode structure including the composite membrane, and lithium secondary battery including the anode structure
US20160190638A1 (en) 2013-09-13 2016-06-30 Toyota Jidosha Kabushiki Kaisha Method for producing sulfide solid electrolyte
US20160190640A1 (en) 2014-12-02 2016-06-30 Polyplus Battery Company VITREOUS SOLID ELECTROLYTE SHEETS OF Li ION CONDUCTING SULFUR-BASED GLASS AND ASSOCIATED STRUCTURES, CELLS AND METHODS
US20170005367A1 (en) 2015-06-24 2017-01-05 Quantumscape Corporation Composite electrolytes
US20170162901A1 (en) 2015-12-04 2017-06-08 Quantumscape Corporation Lithium, phosphorus, sulfur, and iodine including electrolyte and catholyte compositions, electrolyte membranes for electrochemical devices, and annealing methods of making these electrolytes and catholytes
US20170294678A1 (en) * 2016-04-11 2017-10-12 Samsung Electronics Co., Ltd. Composite solid electrolyte, protected anode and lithium battery including the same, and method of preparing the composite solid electrolyte

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE69841343D1 (en) 1997-10-29 2010-01-07 Sony Corp Solid electrolyte cell
JP4355970B2 (en) 1997-10-29 2009-11-04 ソニー株式会社 Solid electrolyte battery and manufacturing method thereof
JP2010040190A (en) 2008-07-31 2010-02-18 Idemitsu Kosan Co Ltd Method for manufacturing pole material slurry
JP5521899B2 (en) 2010-08-26 2014-06-18 トヨタ自動車株式会社 Sulfide solid electrolyte material and lithium solid state battery
JP6234665B2 (en) 2011-11-07 2017-11-22 出光興産株式会社 Solid electrolyte
US10128491B2 (en) * 2011-12-01 2018-11-13 Nanoscale Components, Inc. Method for alkaliating electrodes
US10833366B2 (en) 2012-05-01 2020-11-10 Altairnano, Inc. Lithium titanate cell
JP6003376B2 (en) 2012-08-08 2016-10-05 トヨタ自動車株式会社 Sulfide solid electrolyte glass, lithium solid battery and method for producing sulfide solid electrolyte glass
KR101558669B1 (en) * 2013-10-31 2015-10-07 현대자동차주식회사 A cathode for lithium sulfur battery and a method for preparing thereof
US10312527B2 (en) * 2014-11-10 2019-06-04 Lanxess Solutions Us Inc. Energy storage device comprising a polyurethane separator
HK1247443A1 (en) 2015-02-09 2018-09-21 麻省固能控股有限公司 High salt concentration electrolytes for rechargeable lithium battery
KR102664381B1 (en) 2016-06-21 2024-05-08 삼성전자주식회사 Lithium battery

Patent Citations (151)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4183988A (en) 1978-11-16 1980-01-15 General Electric Company Solid ion-conductive electrolyte
US4357401A (en) 1980-03-31 1982-11-02 L'etat Francais Represente Par Le Delegue General Pour L'armement Macromolecular material of ionic conduction
JPS57108831A (en) 1980-12-26 1982-07-07 Hitachi Maxell Ltd Manufacture of solid electrolytic thin plate
US4668736A (en) 1984-07-18 1987-05-26 Minnesota Mining And Manufacturing Company Fast curing epoxy resin compositions
US4654279A (en) 1986-07-10 1987-03-31 The United States Of America As Represented By The Secretary Of The Navy Interpenetrating-network polymeric electrolytes
US4990587A (en) 1987-06-26 1991-02-05 The Secretary Of State For Defence In Her Britannic Majesty's Government Of The United Kingdom And Northern Ireland Method of preparing toughened epoxy polymers
US4868262A (en) 1987-07-15 1989-09-19 Th. Goldschmidt Ag Copolymers with epoxide groups, their synthesis and use for finishing textile fibers or fiber products
US4990413A (en) 1989-01-18 1991-02-05 Mhb Joint Venture Composite solid electrolytes and electrochemical devices employing the same
US5202009A (en) 1989-10-26 1993-04-13 Compagnie Generale D'electricite Electrolyte solid polymer reticule
US5449576A (en) 1993-11-26 1995-09-12 Motorola, Inc. Multilayered electrolyte and electrochemical cells using same
US6030720A (en) 1994-11-23 2000-02-29 Polyplus Battery Co., Inc. Liquid electrolyte lithium-sulfur batteries
DE19825807A1 (en) 1997-06-10 1998-12-24 Samsung Display Devices Co Ltd A glass-polymer composite electrolyte and a method for producing the same
US6066417A (en) 1997-06-10 2000-05-23 Samsung Display Devices Co., Ltd. Glass-polymer composite electrolyte and a method of preparing the same
US6656641B1 (en) 1997-08-21 2003-12-02 University Of Dayton Methods of enhancing conductivity of a polymer-ceramic composite electrolyte
EP0977296A1 (en) 1997-09-03 2000-02-02 Matsushita Electric Industrial Co., Ltd. Solid electrolytic moldings, electrode moldings, and electrochemical elements
US6200707B1 (en) 1997-09-03 2001-03-13 Matsushita Electric Industrial Co., Ltd. Solid electrolytic moldings, electrode moldings, and electrochemical elements including a polybutadiene block copolymer
US6277524B1 (en) 1997-12-09 2001-08-21 Toyota Jidosha Kabushiki Kaisha Lithium-ion-conductive solid electrolyte and solid-electrolyte lithium battery
US6210836B1 (en) 1998-04-14 2001-04-03 Matsushita Electric Industrial Co., Ltd. Lithium secondary battery
US6365300B1 (en) 1998-12-03 2002-04-02 Sumitomo Electric Industries, Ltd. Lithium secondary battery
JP2001316583A (en) 2000-05-02 2001-11-16 Tsutomu Minami Lithium-ion conductive organic-inorganic composite
US20040096747A1 (en) 2001-01-30 2004-05-20 Andree Schwake Electrolyte solution for electrochemical cells
US20030031931A1 (en) 2001-08-07 2003-02-13 3M Innovative Properties Company Lithium-ion batteries
JP2003217663A (en) 2002-01-16 2003-07-31 Japan Storage Battery Co Ltd Non-aqueous electrolyte battery
US20030157409A1 (en) 2002-02-21 2003-08-21 Sui-Yang Huang Polymer lithium battery with ionic electrolyte
US20030198870A1 (en) 2002-02-27 2003-10-23 Fuji Photo Film Co., Ltd. Electrolytic composition and non-aqueous electrolytic secondary battery
US7915378B2 (en) 2002-04-26 2011-03-29 Hideyuki Nishio Material for solid polymer electrolyte, and polyether polymer and process for producing same
US20050026037A1 (en) 2002-07-26 2005-02-03 A123 Systems, Inc. Bipolar articles and related methods
US20060068296A1 (en) 2002-11-29 2006-03-30 Hiroe Nakagawa Nonaqueous electrolyte and nonaqueous-electrolyte battery
US20110229765A1 (en) 2003-04-03 2011-09-22 Jeremy Barker Electrodes Comprising Mixed Active Particles
US20060166003A1 (en) 2003-06-16 2006-07-27 William Marsh Rice University Fabrication of carbon nanotube reinforced epoxy polymer composites using functionalized carbon nanotubes
US20140170465A1 (en) * 2004-02-06 2014-06-19 Polyplus Battery Company Protected lithium electrodes having a porous electrolyte interlayer and associated battery cells
US8962194B2 (en) 2004-02-12 2015-02-24 Idemitsu Kosan Co., Ltd. Lithium ion conducting sulfide based crystallized glass and method for production thereof
US20070160911A1 (en) 2004-02-12 2007-07-12 Masahiro Tatsumisago Lithium ion conducting sulfide based crystallized glass and method for production thereof
US7416815B2 (en) 2004-04-01 2008-08-26 Sumitomo Electric Industries, Ltd. Negative electrode member for lithium battery and process for producing the same
US20080131781A1 (en) 2004-08-17 2008-06-05 Lg Chem, Ltd. Lithium Secondary Batteries With Enhanced Safety And Performance
US20090208806A1 (en) 2005-02-15 2009-08-20 Toray Industries, Inc. Method for producing polymer electrolyte molded article, polymer electrolyte material, polymer electrolyte membrane, and polymer electrolyte fuel cell
US20060216603A1 (en) 2005-03-26 2006-09-28 Enable Ipc Lithium-ion rechargeable battery based on nanostructures
US20060246355A1 (en) 2005-04-27 2006-11-02 Samsung Sdi Co., Ltd. Lithium secondary battery
US20070015022A1 (en) 2005-07-12 2007-01-18 Samsung Sdi Co., Ltd. Ion conductive composite membrane using inorganic conductor and method of manufacturing the same
US20080200589A1 (en) 2005-07-15 2008-08-21 Huntsman International Llc Toughened Composition
US20100151335A1 (en) 2005-08-02 2010-06-17 Idemitsu Kosan Co., Ltd. Solid electrolyte sheet
CN1925203A (en) 2005-08-31 2007-03-07 株式会社小原 Lithium ion secondary battery and solid electrolyte therefor
CN1949569A (en) 2005-10-13 2007-04-18 株式会社小原 Lithium ion conductive solid electrolyte and method for manufacturing the same
US20070117026A1 (en) 2005-11-21 2007-05-24 Binod Kumar Solid composite electrolyte membrane and method of making
US20070117007A1 (en) 2005-11-23 2007-05-24 Polyplus Battery Company Li/air non-aqueous batteries
US20070172739A1 (en) 2005-12-19 2007-07-26 Polyplus Battery Company Composite solid electrolyte for protection of active metal anodes
US20150287986A1 (en) 2006-03-22 2015-10-08 Sion Power Corporation Electrode protection in both aqueous and non-aqueous electrochemical cells, including rechargeable lithium batteries
US20070231704A1 (en) 2006-03-30 2007-10-04 Ohara Inc. Lithium ion conductive solid electrolyte and production process thereof
JP2007273217A (en) 2006-03-31 2007-10-18 Idemitsu Kosan Co Ltd Solid electrolyte, method for producing the same, and all-solid-state secondary battery
JP2007273214A (en) 2006-03-31 2007-10-18 Idemitsu Kosan Co Ltd Solid electrolyte, method for producing the same, and all-solid-state secondary battery
US7901598B2 (en) 2006-05-15 2011-03-08 Sumitomo Electric Industries, Ltd. Solid electrolyte and method of producing the same
US20080220334A1 (en) 2006-10-31 2008-09-11 Ohara Inc. Lithium ion conductive solid electrolyte and a method for manufacturing the same
CN101174698A (en) 2006-10-31 2008-05-07 株式会社小原 Lithium ion conductive solid electrolyte and a method for manufacturing the same
US20090226816A1 (en) 2006-11-14 2009-09-10 Ngk Insulators, Ltd. Solid electrolyte structure for all-solid-state battery, all-solid-state battery, and their production methods
US20100019194A1 (en) 2006-12-26 2010-01-28 Tetsu Fujiwara Positive electrode active material for nonaqueous electrolyte secondary battery, positive electrode and secondary battery
CN101542777A (en) 2007-02-05 2009-09-23 Lg化学株式会社 Organic/inorganic composite separator having porous active coating layer and electrochemical device comprising the same
CN101013761A (en) 2007-02-13 2007-08-08 中国科学院上海硅酸盐研究所 Solid electrolyte material system for all solid state lithium battery and preparation method
US20100028768A1 (en) 2007-08-02 2010-02-04 Sony Corporation Positive electrode active material, positive electrode using the same and non-aqueous electrolyte secondary battery
CN101425604A (en) 2007-09-05 2009-05-06 精工爱普生株式会社 Solid electrolyte material, battery device and all-solid lithium secondary battery
US20090087751A1 (en) 2007-09-05 2009-04-02 Seiko Epson Corporation Solid electrolyte material of conducting lithium ion, battery device using the solid electrolyte material and all-solid lithium secondary battery provided with the battery device
US20090136830A1 (en) 2007-11-27 2009-05-28 John Howard Gordon Substantially Solid, Flexible Electrolyte For Alkili-Metal-Ion Batteries
US20090182066A1 (en) 2007-12-27 2009-07-16 E. I. Du Pont De Nemours And Company Crosslinkable fluoropolymer, crosslinked fluoropolymers and crosslinked fluoropolymer membranes
JP2009176541A (en) 2008-01-23 2009-08-06 Idemitsu Kosan Co Ltd Solid electrolyte membrane, positive electrode membrane, or negative electrode membrane for all solid lithium secondary battery, method for producing the same, and all solid lithium secondary battery
US20120196186A1 (en) 2008-06-20 2012-08-02 Toyota Motor Engineering & Manufacturing North America, Inc. Electrode material with core-shell structure
CN102106030A (en) 2008-07-23 2011-06-22 丰田自动车株式会社 Polymer electrolyte membrane, method for producing polymer electrolyte membrane, and solid polymer fuel cell
US20110311875A1 (en) 2008-11-20 2011-12-22 Lg Chem, Ltd. Electrode active material for secondary battery and method for preparing the same
US8546019B2 (en) 2008-11-20 2013-10-01 Lg Chem, Ltd. Electrode active material for secondary battery and method for preparing the same
US20120208062A1 (en) 2008-12-26 2012-08-16 Haoshen Zhou Lithium secondary cell
US20110262816A1 (en) 2009-01-12 2011-10-27 Glenn Amatucci Polyhydrogen fluoride based battery
US20100183924A1 (en) 2009-01-22 2010-07-22 Hanwha Chemical Corporation Electrode-active anion-deficient non-stoichiometric lithium iron phosphate, method for preparing the same, and electrochemical device using the same
US20120094185A1 (en) 2009-05-01 2012-04-19 Toyota Jidosha Kabushiki Kaisha Solid electrolyte material, electrode element that includes solid electrolyte material, all-solid battery that includes solid electrolyte material, and manufacturing method for solid electrolyte material
JP2011044249A (en) 2009-08-19 2011-03-03 Toyota Motor Corp Sulfide solid electrolyte material
US8729866B2 (en) 2009-09-02 2014-05-20 Toyota Jidosha Kabushiki Kaisha Sulfide-based all-solid-state lithium secondary battery system
US20110076570A1 (en) 2009-09-29 2011-03-31 Toyota Jidosha Kabushiki Kaisha Solid state electrolyte layer, electrode active material layer, all solid state lithium battery, manufacturing method for solid state electrolyte layer, and manufacturing method for electrode active material layer
US20110259505A1 (en) 2009-09-29 2011-10-27 Lg Chem, Ltd. Method for manufacturing separator, separator manufactured therefrom and method for manufacturing electrochemical device having the same
US20120244411A1 (en) 2009-10-02 2012-09-27 Sumitomo Chemical Company, Limited Lithium-containing metal oxide, and non-aqueous electrolyte secondary battery
US8524393B2 (en) 2009-11-25 2013-09-03 Toyota Jidosha Kabushiki Kaisha Method for producing electrode laminate and electrode laminate
US20120115763A1 (en) 2009-12-30 2012-05-10 Exxonmobil Research And Engineering Company Lubricant compositions based on block copolymers and processes for makin
US8697292B2 (en) 2010-03-26 2014-04-15 Tokyo Institute Of Technology Sulfide solid electrolyte material, battery, and method for producing sulfide solid electrolyte material
US20130040208A1 (en) 2010-03-26 2013-02-14 Toyota Jidosha Kabushiki Kaisha Sulfide solid electrolyte material, battery, and method for producing sulfide solid electrolyte material
US9252455B1 (en) * 2010-04-14 2016-02-02 Hrl Laboratories, Llc Lithium battery structures employing composite layers, and fabrication methods to produce composite layers
US9172112B2 (en) 2010-08-05 2015-10-27 Toyota Jidosha Kabushiki Kaisha Sulfide solid electrolyte glass, lithium solid state battery and producing method of sulfide solid electrolyte glass
JP2012054212A (en) 2010-09-03 2012-03-15 Toyota Motor Corp Sulfide solid electrolyte material, method for producing sulfide solid electrolyte material, and lithium solid battery
US20130216910A1 (en) 2010-11-09 2013-08-22 3M Innovative Properties Company High capacity alloy anodes and lithium-ion electrochemical cells containing same
US20140023940A1 (en) 2010-12-01 2014-01-23 Hydro-Quebec Lithium-air battery
JP2012146512A (en) 2011-01-12 2012-08-02 Toyota Motor Corp Method for manufacturing battery
US20120276459A1 (en) 2011-04-29 2012-11-01 National University Corporation Mie University Negative electrode for lithium secondary battery, method of manufacturing the same, and lithium secondary battery employing the same
US20140093785A1 (en) 2011-05-18 2014-04-03 Toyota Jidosha Kabushiki Kaisha Method of producing solid sulfide electrolyte material and solid sulfide electrolyte material
WO2012156795A8 (en) 2011-05-18 2013-01-17 Toyota Jidosha Kabushiki Kaisha Method of producing solid sulfide electrolyte material and solid sulfide electrolyte material
WO2012156795A1 (en) 2011-05-18 2012-11-22 Toyota Jidosha Kabushiki Kaisha Method of producing solid sulfide electrolyte material and solid sulfide electrolyte material
JP2013012416A (en) 2011-06-29 2013-01-17 Sumitomo Electric Ind Ltd Nonaqueous electrolyte battery and nonaqueous electrolyte battery manufacturing method
US20130004843A1 (en) 2011-06-29 2013-01-03 Hitachi, Ltd. Electrode for lithium ion battery, manufacturing method thereof, lithium ion battery, and manufacturing method thereof
US9172113B2 (en) 2011-07-06 2015-10-27 Toyota Jidosha Kabushiki Kaisha Sulfide solid electrolyte material, lithium solid-state battery, and method for producing sulfide solid electrolyte material
US20140141341A1 (en) 2011-07-06 2014-05-22 Toyota Jidosha Kabushiki Kaisha Sulfide solid electrolyte material, lithium solid-state battery, and method for producing sulfide solid electrolyte material
US20140197800A1 (en) 2011-07-26 2014-07-17 Toyota Jidosha Kabushiki Kaisha Lithium solid state secondary battery system
JP2013045683A (en) 2011-08-25 2013-03-04 Sumitomo Electric Ind Ltd Electrode for solid electrolyte battery, solid electrolyte layer, solid electrolyte battery, and binder used for the same
US20130052509A1 (en) 2011-08-25 2013-02-28 GM Global Technology Operations LLC Lithium ion battery with electrolyte-embedded separator particles
JP2013080616A (en) 2011-10-04 2013-05-02 Seiko Epson Corp Lithium ion secondary battery and method of manufacturing wound body
US20130095358A1 (en) 2011-10-13 2013-04-18 Eveready Battery Company, Inc. Lithium Iron Disulfide Battery
US20130108934A1 (en) 2011-10-27 2013-05-02 National University Corporation Mie University Electrolyte for lithium air battery and lithium air battery including the same
CN104011926A (en) 2011-11-02 2014-08-27 I-Ten公司 Method for preparing solid electrolyte film for lithium ion battery
US20140363745A1 (en) 2011-12-22 2014-12-11 Toyota Jidosha Kabushiki Kaisha Sulfide solid electrolyte material, battery, and producing method for sulfide solid electrolyte material
US20150037687A1 (en) 2012-02-06 2015-02-05 Tokyo Institute Of Technology Sulfide solid electrolyte material, battery, and producing method for sulfide solid electrolyte material
US20150017548A1 (en) 2012-02-06 2015-01-15 Toyota Jidosha Kabushiki Kaisha Sulfide solid electrolyte material, battery, and producing method for sulfide solid electrolyte material
WO2013125485A1 (en) 2012-02-24 2013-08-29 住友電気工業株式会社 All-solid-state lithium secondary battery
CN104159869A (en) 2012-03-02 2014-11-19 日本碍子株式会社 Solid electrolyte ceramic material and production method therefor
US20130230778A1 (en) 2012-03-02 2013-09-05 Honda Motor Co., Ltd. Lithium ion conductive composite electrolyte and lithium ion secondary battery using same
US20140193695A1 (en) 2012-03-13 2014-07-10 Kabushiki Kaisha Toshiba Lithium-ion conducting oxide, solid electrolyte secondary battery and battery pack
US20140193693A1 (en) 2012-03-16 2014-07-10 Kabushiki Kaisha Toshiba Lithium-ion conductive sulfide, solid electrolyte secondary battery and battery pack
US20150085423A1 (en) 2012-04-18 2015-03-26 The Arizona Board Of Regents, A Body Corporate Act For And On Behalf Of Structural Supercapacitors
US20150111110A1 (en) 2012-04-27 2015-04-23 Kabushiki Kaisha Toyota Jidoshokki Solid electrolyte and secondary battery
US8871391B2 (en) 2012-05-03 2014-10-28 Ut-Battelle, Llc Lithium sulfide compositions for battery electrolyte and battery electrode coatings
JP2014038755A (en) 2012-08-14 2014-02-27 Toyota Motor Corp Manufacturing method of sulfide solid electrolytic material
US20140065513A1 (en) 2012-08-29 2014-03-06 Michael Edward Badding Ion-conducting composite electrolyte comprising path-engineered particles
US20140072866A1 (en) * 2012-09-12 2014-03-13 Sony Corporation Secondary battery, battery pack, and electric vehicle
WO2014073197A1 (en) 2012-11-06 2014-05-15 出光興産株式会社 Solid electrolyte
US20140170504A1 (en) 2012-12-14 2014-06-19 Samsung Electronics Co., Ltd. Flexible solid electrolyte, all-solid-state lithium battery including the flexible solid electrolyte, and method of preparing the flexible solid electrolyte
KR20140095658A (en) 2013-01-24 2014-08-04 엘지전자 주식회사 Solar cell
EP2983231A1 (en) 2013-04-02 2016-02-10 Idemitsu Kosan Co., Ltd. Composite material
WO2014186634A2 (en) 2013-05-15 2014-11-20 Quantumscape Corporation Solid state catholyte or electrolyte for battery using liampbsc (m = si, ge, and/or sn)
US10535878B2 (en) 2013-05-15 2020-01-14 Quantumscape Corporation Solid state catholyte or electrolyte for battery using LiaMPbSc (M=Si, Ge, and/or Sn)
US9819024B2 (en) 2013-05-15 2017-11-14 Quantumscape Corporation Solid state catholytes and electrolytes for energy storage devices
US9634354B2 (en) 2013-05-15 2017-04-25 Quantumscape Corporation Solid state catholytes and electrolytes for energy storage devices
US9553332B2 (en) 2013-05-15 2017-01-24 Quantumscape Corporation Solid state catholytes and electrolytes for energy storage devices
US9172114B2 (en) 2013-05-15 2015-10-27 Quantumscape Corporation Solid state catholytes and electrolytes for energy storage devices
US11139479B2 (en) 2013-05-15 2021-10-05 Quantumscape Battery, Inc. Solid state catholyte or electrolyte for battery using LiaMPbSc (M=Si, Ge, and/or Sn)
US11211611B2 (en) 2013-05-15 2021-12-28 Quantumscape Battery, Inc. Solid state catholyte or electrolyte for battery using LiaMPbSc (M=Si, Ge, and/or Sn)
JP2014241240A (en) 2013-06-12 2014-12-25 トヨタ自動車株式会社 Method for manufacturing sulfide all-solid battery
US20160164136A1 (en) 2013-07-04 2016-06-09 Mitsui Mining & Smelting Co., Ltd. Crystalline solid electrolyte and production method therefor
US20150056496A1 (en) 2013-08-23 2015-02-26 Ut-Battelle, Llc Lithium-conducting sulfur compound cathode for lithium-sulfur batteries
JP2015050072A (en) 2013-09-02 2015-03-16 日本碍子株式会社 Solid electrolyte ceramic materials
US20160190638A1 (en) 2013-09-13 2016-06-30 Toyota Jidosha Kabushiki Kaisha Method for producing sulfide solid electrolyte
US20150099190A1 (en) * 2013-10-07 2015-04-09 Quantumscape Corporation Garnet materials for li secondary batteries and methods of making and using garnet materials
US20150200420A1 (en) 2013-10-07 2015-07-16 Quantumscape Corporation Garnet materials for li secondary batteries and methods of making and using garnet materials
US20150118574A1 (en) 2013-10-31 2015-04-30 Samsung Electronics Co., Ltd. Positive electrode for lithium-ion secondary battery, and lithium-ion secondary battery
US20150171463A1 (en) 2013-12-12 2015-06-18 Ut-Battelle, Llc High conducting oxide - sulfide composite lithium superionic conductor
CN104143656A (en) 2014-07-04 2014-11-12 中南大学 A kind of preparation method of inorganic solid electrolyte membrane/electrode composite material
CN104377385A (en) 2014-09-26 2015-02-25 珠海光宇电池有限公司 Lithium ion secondary battery composite electrolyte film, and making method and application thereof
CN104538670A (en) 2014-11-24 2015-04-22 深圳华中科技大学研究院 All-solid polymer electrolyte, and preparation method and application of all-solid polymer electrolyte
US20160156065A1 (en) 2014-12-02 2016-06-02 Polyplus Battery Company Standalone sulfide based lithium ion-conducting glass solid electrolyte and associated structures, cells and methods
US20160190640A1 (en) 2014-12-02 2016-06-30 Polyplus Battery Company VITREOUS SOLID ELECTROLYTE SHEETS OF Li ION CONDUCTING SULFUR-BASED GLASS AND ASSOCIATED STRUCTURES, CELLS AND METHODS
US20160181585A1 (en) 2014-12-19 2016-06-23 Samsung Electronics Co., Ltd. Composite membrane, preparation method thereof, anode structure including the composite membrane, and lithium secondary battery including the anode structure
US20200067137A1 (en) 2015-06-24 2020-02-27 Quantumscape Corporation Composite electrolytes
US20170005367A1 (en) 2015-06-24 2017-01-05 Quantumscape Corporation Composite electrolytes
US11145898B2 (en) 2015-06-24 2021-10-12 Quantumscape Battery, Inc. Composite electrolytes
US10374254B2 (en) 2015-06-24 2019-08-06 Quantumscape Corporation Composite electrolytes
US20190097262A1 (en) 2015-12-04 2019-03-28 Quantumscape Corporation Lithium, phosphorus, sulfur, and iodine including electrolyte and catholyte compositions, electrolyte membranes for electrochemical devices, and annealing methods of making these electrolytes and catholytes
US10826115B2 (en) 2015-12-04 2020-11-03 Quantumscape Corporation Lithium, phosphorus, sulfur, and iodine including electrolyte and catholyte compositions, electrolyte membranes for electrochemical devices, and annealing methods of making these electrolytes and catholytes
US10116001B2 (en) 2015-12-04 2018-10-30 Quantumscape Corporation Lithium, phosphorus, sulfur, and iodine including electrolyte and catholyte compositions, electrolyte membranes for electrochemical devices, and annealing methods of making these electrolytes and catholytes
US20170162901A1 (en) 2015-12-04 2017-06-08 Quantumscape Corporation Lithium, phosphorus, sulfur, and iodine including electrolyte and catholyte compositions, electrolyte membranes for electrochemical devices, and annealing methods of making these electrolytes and catholytes
US20170294678A1 (en) * 2016-04-11 2017-10-12 Samsung Electronics Co., Ltd. Composite solid electrolyte, protected anode and lithium battery including the same, and method of preparing the composite solid electrolyte

Non-Patent Citations (166)

* Cited by examiner, † Cited by third party
Title
Adams, S. et al., "Structural requirements for fast lithium ion migration in Li10GeP2S12", J. Mater. Chem., 2012, 22, pp. 7687-7691.
Aetukuri, Nagaphani B. et al., "Flexible Ion-Conducting Composite Membranes for Lithium Batteries," Adv. Energy Mater., 2015, 1500265, 6 pages.
Ahn, Byung Tae, et al., "Synthesis and Lithium Conductivities of Li2SiS3and Li4SiS4", Mat. Res. Bull., 1989, vol. 24, pp. 889-897.
Aihara, Yuichi et al., "The electrochemical characteristics and applicability of an amorphous sulfide based solid ion conductor for the next generation solid-state lithium secondary batteries", Front. Energy Res., May 13, 2016, pp. 1-8.
Amaresh, S. et al., "Aluminum based sulfide solid lithium ionic conductors for all solid state batteries," Nanoscale, 2014, vol. 6, pp. 6661-6667.
Andrews, Lester, et al., "Infrared Spectra of P4S10 and its Decomposition Products in Solid Argon," Inorganic Chemistry, 1990, vol. 29, pp. 5222-5225.
Anonymous, "A Binding Matter," Ceramic Industry Magazine, Oct. 1, 2001, 6 pages; website: http://www.ceramicindustry.com/articles/82746-a-binding-matter.
Aotani, Noboru, "Synthesis and electrochemical properties of lithium ion conductive glass, Li3PO4—Li2—S—SiS2", Solid State Ionics, 1994, vol. 68, pp. 35-39.
Bartholomew et al., "Electrical properties of new glasses based on the Li2S—SiS2 system", Journal of Non-Crystalline Solids, 1999, vol. 256 & 257, pp. 242-247.
Bhandari et al., "Origin of Fast Ion Conduction in Li10GeP2S12, a Superionic Conductor", J. Phys. Chem. C, 2016, vol. 120, pp. 29002-29010.
Blanga, R. et al., "The search for a solid electrolyte, as a polysulfide barrier, for lithium/sulfur batteries", J Solid State Electrochem, Jul. 2016, 12 pages.
Boyle, Maureen A. et al., "Epoxy Resins", ASM Handbook, vol. 21, Composites, 2001, pp. 79-89.
Bron, P. et al., "Li10Si0.3Sn0.7P2S12—A low-cost and low-grain-boundary-resistance lithium superionic conductor", Journal of Power Sources, vol. 329, 2016, pp. 530-535.
Bron, P. et al., "Li10SnP2S12: An Affordable Lithium Superionic Conductor", J. Am. Chem. Soc., 2013, vol. 135, pp. 15694-15697.
Camino et al., "Polydimethylsiloxane thermal degradation Part 1. Kinetic aspects", Polymer, vol. 42, No. 6, Mar. 2001, pp. 2395-2402.
Chen et al., "A new composite solid electrolyte PEO/Li10GeP2S12/SN for all-solid-state lithium battery," Electrochimica Acta, vol. 210, 2016, pp. 905-914.
Chen, M.-H., "Update on Dental Nanocomposites", J Dent Res, 2010, 89(6), pp. 549-560.
Cramer, N.B. et al., "Recent Advances and Developments in Composite Dental Restorative Materials", J Dent Res, 2011, 90(4), pp. 402-416.
Creus et al., "The Use of Ionic and Mixed Conductive Glasses in Microbatteries", Materials Science and Engineering, 1989, B3, pp. 109-112.
Creus et al., "Thin films of ionic and mixed conductive glasses: their use in microdevices", Solid State Ionics, 1992, vol. 53-56, pp. 641-646.
Croce, F. et al., "Physical and Chemical Properties of Nanocomposite Polymer Electrolytes", J. Phys. Chem. B, 1999, 103, pp. 10632-10638.
De Klerk, Niek J.J. et al., "Diffusion Mechanism of Li Argyrodite Solid Electrolytes for Li-Ion Batteries and Prediction of Optimized Halogen Doping: The Effect of Li Vacancies, Halogens, and Halogen Disorder", Chem. Mater. 2016, vol. 28, pp. 7955-7963.
Deiseroth, Hans-Jorg, et al., "Li6PS5X: A Class of Crystalline Li Rich Solids with an Unusually High Li+ Mobility," Angew. Chem. Int. Ed., 2008, vol. 47, pp. 755-758.
Du et al., "Structures, Thermodynamics, and Li+ Mobility of Li10GeP2S12: A First-Principles Analysis", J. Phys. Chem. C 2014, vol. 118, pp. 10590-10595.
Duffy et al., "Electroless deposition and characterization of Fe/FeOx nanoparticles on porous carbon microspheres: structure and surface reactivity", J. Mater. Chem A, 2013, vol. 1, pp. 6043-6050.
Duluard et al., "Lithium conducting solid electrolyte Li13Al53Ti17(PO4)3 obtained via solution chemistry", Journal of the European Ceramic Society, 2013, vol. 33, pp. 1145-1153.
Eckert et al., "Structural Transformation of Non-Oxide Chalcogenide Glasses. The Short-Range Order of Li2S—P2S5 Glasses Studied by Quantitative 31P and 6,7Li High-Resolution Solid-State NMR," Chem. Mater., 1990, vol. 2, pp. 273-279.
English translation of the third office action of Chinese Patent application No. 201680036919.3 dated Jul. 5, 2021.
Extended European Search Report for EP Application No. 16871533.2 dated Jun. 26, 2019, 10 pages.
Fu, Kun (Kelvin) et al., "Flexible, solid-state, ion-conducting membrane with 3D garnet nanofiber networks for lithium batteries", PNAS, vol. 113, No. 26, 2016, pp. 7094-7099.
Goodman, Sidney H., "Epoxy Resins", Handbook ofThermoset Plastics, 1999, pp. 193-268.
Hassoun et al., "A structural, spectroscopic and electrochemical study of a lithium ion conducting Li10GeP2S12 solid electrolyte", Journal of Power Sources, 229, 2013, pp. 117-122.
Hayashi, Akitoshi, et al., "Characterization of Li2S—P2S5 glass-ceramics as a solid electrolyte for lithium secondary batteries", Solid State Ionics, 2004, vol. 175, pp. 683-686.
Hayashi, Akitoshi, et al., "Characterization of Li2S—SiS2Li3MO3 (M=B, A1, Ga and In) oxysulfide glasses and their application to solid state lithium secondary batteries," Solid State Ionics, 2002, vol. 152-153, pp. 285-290.
Hayashi, Akitoshi, et al., "Development of sulfide glass-ceramic electrolytes for all-solid-state lithium rechargeable batteries", J. Solid State Electrochem, 2010, vol. 14, pp. 1761-1767.
Hayashi, Akitoshi, et al., "Formation of Li superionic crystals from the Li2S—P2S5melt-quenched glasses", J. Mater Sci, 2008, vol. 43, pp. 1885-1889.
Hayashi, Akitoshi, et al., "Formation of superionic crystals from mechanically milled Li2S—P2S5 glasses", Electrochemistry Communications, 2003, vol. 5, pp. 111-114.
Hayashi, Akitoshi, et al., "Improvement of chemical stability of Li3PS4 glass electrolytes by adding MA (M=Fe, Zn, and Bi) nanoparticles", Journal of Materials Chemistry A, 2013, vol. 1, pp. 6320-6326.
Hayashi, Akitoshi, et al., "Preparation of Li2S—P2S5 Amorphous Solid Electrolytes by Mechanical Milling," Journal of the American Ceramic Society, 2001, vol. 84, pp. 477-479.
Hirai, Koichi, et al., "Thermal and electrical properties of rapidly quenched glasses in the systems LI2S—SiS2—LixMOy (LixMOy=LixSiO4, Li2SP4)", Solid State Ionics, 1995, vol. 78, pp. 269-273.
Hu, C.H. et al., "Insights into structural stability and Li superionic conductivity of Li10GeP2S12 from first-principles calculations", Chemical Physics Letters, vol. 591, 2014, pp. 16-20.
Hu, Y-W., et al., "Ionic Conductivity of Lithium Orthosilicate-Lithium Phosphate Solid Solutions", J. Electrochem. Soc., 1977, vol. 124, No. 8, pp. 1240-1242.
Inada, T. et al., "All solid-state sheet battery using lithium inorganic solid electrolyte, thio-LISICON", Journal of Power Sources, vol. 194, 2009, pp. 1085-1088.
Inada, T. et al., "Fabrications and properties of composite solid-state electrolytes", Solid State Ionics, vol. 158, 2003, pp. 275-280.
Inada, T. et al., "Silicone as a binder in composite electrolytes", Journal of Power Sources, vol. 119-121, 2003, pp. 948-950.
International Search Report and Written Opinion of PCT/US2014/038283 dated Nov. 17, 2014, 17 pages.
International Search Report and Written Opinion of PCT/US2016/039424 dated Nov. 3, 2016, 15 pages.
International Search Report and Written Opinion of PCT/US2016/064492 dated Feb. 7, 2017, 13 pages.
International Search Report and Written Opinion of PCT/US2017/049218 dated Jan. 4, 2018, 15 pages.
Kaib, Thomas, et al., "New Lithium Chalcogenidotetrelates, LiChT: Synthesis and Characterization of the LitConducting Tetralithium ortho-Sulfidostannate Li4SnS4", Chemistry of Materials, 2012, vol. 24, pp. 2211-2219.
Kamaya, Noriaki, et al., "A lithium superionic conductor," Nature Materials, Sep. 2011, vol. 10, pp. 682-686; and Supplementary Information, DOI:10.1038/NMAT3066, 3 pages.
Kang, Joonhee et al., "First-Principles Characterization of the Unknown Crystal Structure and Ionic Conductivity of Li7P2S8I as a Solid Electrolyte for High-Voltage Li Ion Batteries", J. Phys. Chem. Letters, 2016, vol. 7, pp. 2671-2675.
Kanno, R. et al., "New Lithium Solid Electrolytes, Thio-Lisicon: Materials Design Concept and Application to Solid State Battery", Solid State Ionics: Trends In The New Millennium, Dec. 7, 2002, pp. 13-22.
Kanno, Ryoji, "Lithium Ionic Conductor Thio-LISICON, the Li2S—GeS2—P2S5 System", Journal of the Electrochemical Society, 2001, vol. 148, pp. A742-A746.
Kanno, Ryoji, "Synthesis of a new lithium ionic conductor, thio-LISICON-lithium germanium sulfide system," Solid State Ionics, 2000, vol. 130, pp. 97-104.
Kato, Y. et al., "Discharge Performance of All-Solid-State Battery Using a Lithium Superionic Conductor Li10GeP2S12", Electrochemistry, vol. 80, No. 10, 2012, pp. 749-751.
Kato, Y. et al., "Synthesis, structure and lithium ionic conductivity of solid solutions of Li10(Ge1-xMx)P2S12 (M=Si, Sn)," Journal of Power Sources, 271, 2014, pp. 60-64.
Kennedy, John, H., et al., "A Highly Conductive Li+-Glass System: (1-x) (0.4SiS2—0.6Li2S)-xLil", J. Electrochem. Soc., 1986, pp. 2437-2438.
Kobayashi, Takeshi, et al., "Interfacial reactions at electrode/electrolyte boundary in all solid-state lithium battery using inorganic solid electrolyte, thio-LISICON", Electrochimica Acta, 2008, vol. 53, pp. 5045-5050.
Koh et al., "Synthesis of lithium-beta-alumina by various ion-exchange and conversion processes", Solid State Ionics, vol. 220, 2012, pp. 32-38.
Kondo, S., et al., "New lithium ion conductors based on Li2S—SiS2 system", Solid State Ionics, vol. 53-56, 1992, pp. 1183-1186.
Kuhn, A. et al., "A new ultrafast superionic Li-conductor: ion dynamics in Li11Si2PS12 and comparison with other tetragonal LGPS-type electrolytes", Phys. Chem. Chem. Phys., 2014, 16, pp. 14669-14674.
Kuhn, A. et al., "Single-crystal X-ray structure analysis of the superionic conductor Li10GeP2S12", Phys. Chem. Chern. Phys., 2013, vol. 15, pp. 11620-11622.
Kuhn, A. et al., "Tetragonal Li10GeP2S12 and Li7GePS8—exploring the Li ion dynamics in LGPS Li electrolytes", Energy Environ. Sci., 2013, vol. 6, pp. 3548-3552.
Kuhn, A. et al., "Ultrafast Li Electrolytes Based on Abundant Elements: Li10SnP2S12 and Li11Si2PS12", Supporting Information, Feb. 19, 2014: arXiv: 1402.4586; 9 pages.
Kuhn, A. et al., "Ultrafast Li Electrolytes Based on Abundant Elements: Li10SNP2S12and Li11Si2PS12," Feb. 19, 2014: arXiv: 1402.4586; 7 pages.
Kumar et al., "Composite Electrolytes for Lithium Rechargeable Batteries", Journal of Electroceramics, 2000, vol. 5:2, pp. 127-139.
Langer, Frederieke et al., "Microstructure and temperature dependent lithium ion transport of ceramic-polymer composite electrolyte for solid-state lithium ion batteries based on garnet-type Li7La3Zr2O12", Solid State Ionics, 2016, vol. 291, pp. 8-13.
Leal-Gonzalez, J., et al., "Structure of Lithium Sulfide, LiGaS2," Acta. Cryst., 1990, pp. 2017-2019.
Li, Qin et al., "Atomistic investigation of the nanoparticle size and shape effects on ionic conductivity of solid polymer electrolytes," Solid State Ionics, 268, 2014, pp. 156-161.
Lim, Young Jun et al., "Ceramic-Based Composite Solid Electrolyte for Lithium-Ion Batteries", 2015, vol. 80, pp. 1100-1103.
Liu, Wei et al., "Ionic Conductivity Enhancement of Polymer Electrolytes with Ceramic Nanowire Fillers," Nano Lett., 2015, 15 (4), pp. 2740-2745.
Liu, Zengcai, et al., "Anomalous High Iconic Conductivity of Nanoporous R-Li3PS4, Journal of the American Chemical Society", 2012, 4 pages.
Liu, Zhangiang, et al., "High performance Li2S-P2S5 solid electrolyte induced by selenide", Journal of Power Sources, 2014, vol. 260, pp. 264-267.
Mcgrogan, Frank P. et al., "Compliant Yet Brittle Mechanical Behavior of Li2S—P2S5 Lithium-Ion-Conducting Solid Electrolyte", Adv. Energy Mater., 2017, 1602011, 5 pages; DOI: 10.1002/aenm.201602011.
Menetrier, M, et al., "Iconic conduction in B2S3—Li2S—Lil glasses", Solid State Ionics, 1992, vol. 53-56, pp. 1208-1213.
Menetrier, M. et al., "Electrochemical Properties of B2S3—Li2S—Lil Vitreous Electrolytes", J. Electrochem. Soc, 1984, 131(9), pp. 1971-1973.
Mercier, Rene, et al., "Superionic Conduction in Li2S—P2S5—Lil-Glasses", Solid State Ionics, 1981, vol. 5, pp. 663-666.
Minami, Keiichi, et al., "Electrical and electrochemical properties of glass-ceramic electrolytes in the systems Li2S—P2S5—P2S3 and Li2S—P2S5—P2O5", Solid State Ionics, 2011, vol. 192, pp. 122-125.
Minami, Keiichi, et al., "Electrical and electrochemical properties of the 70Li2S·(30-x)P2S5·xP2O5 glass-ceramic electrolytes", Solid State Ionics, 2008, vol. 179, pp. 1282-1285.
Minami, Keiichi, et al., "Lithium ion conductivity of the Li2S—P2S5 glass-based electrolytes prepared by the melt quenching method", Solid State Ionics, 2007, vol. 178, pp. 837-841.
Minami, Tsutomu, "Fast Ion Conducting Glasses, Journal of Non-Crystalline Solids", 1985, vol. 73, pp. 273-284.
Minami, Tsutomu, et al., "Preparation and characterization of lithium ion-conducting oxysulfide glasses", Solid State Ionics, 2000, vol. 136-137, pp. 1015-1023.
Minami, Tsutomu, et al., "Recent progress of glass and glass-ceramics as solid electrolytes for lithium secondary batteries", Solid State Ionics, 2006, vol. 177, pp. 2715-2720.
Mizuno, Fuminori, et al., "All Solid-State Lithium Secondary Batteries Using High Lithium Ion Conducting Li2S—P2S5 Glass-Ceramics," Chemistry Letters, 2002, pp. 1244-1245.
Mizuno, Fuminori, et al., "High lithium ion conducting glass-ceramics in the system Li2S—P2S5", Solid State Ionics, 2006, vol. 177, pp. 2721-2725.
Mizuno, Fuminori, et al., "New, Highly Ion-Conductive Crystals Precipitated from Li2S—P2S5 Glasses", Advanced Materials, 2005, vol. 17, No. 7, pp. 918-921.
Mo et al., "First Principles Study of the Li10GeP2S12 Lithium Super Ionic Conductor Material", Chem. Mater., 2012, vol. 24, pp. 15-17.
Morimoto, Hideyuki, et al., "Mechanochemical Synthesis of New Amorphous Materials of 60Li2S—40SiS2 with High Lithium Ion Conductivity", J. Am. Ceram. Soc., 1999, vol. 82, pp. 1352-1354.
Muramatsu, Hiromasa, et al., "Structural change of Li2S—P2S5 sulfide solid electrolytes in the atmosphere", Solid State Ionics, 2011, vol. 182, pp. 116-119.
Murayama, Masahiro, et al., "Material Design of New Lithium Ionic Conductor thio-LISICON, in the Li2S—P2S5 System," Solid State Ionics, 2004, vol. 170, pp. 173-180.
Murayama, Masahiro, et al., "Synthesis of New Lithium Ionic Conductor Thio-LISICON-Lithium Silicon Sulfides System", Journal of Solid State Chemistry, 2002, vol. 168, pp. 140-148.
Nairn, K. et al., "Ceramic-polymer interface in composite electrolytes of lithium aluminium titanium phosphate and polyetherurethane polymer electrolyte", Solid State Ionics, vol. 121, 1999, pp. 115-119.
Nairn, K. et al., "Polymer-ceramic ion-conducting composites", Solid State Ionics, vol. 86-88, 1996, pp. 589-593.
Nam, Young Jin et al., "Bendable and Thin Sulfide Solid Electrolyte Film: A New Electrolyte Opportunity for Free Standing and Stackable High-Energy All-Solid-State Lithium-Ion Batteries", Nano Lett., 2015, 15 (5), pp. 3317-3323.
Nam, Young Jin et al., Supporting Information "Bendable and Thin Sulfide Solid Electrolyte Film: A New Electrolyte Opportunity for Free Standing and Stackable High-Energy All-Solid-State Lithium-Ion Batteries", Nano Lett., 2015, 15 (5), pp. 3317-3323.
Norrel et al., "Anion exchange of Oxygen by Sulfur in GeO2-based glasses", Proceedings of SPIE, vol. 4990, 2003, pp. 87-96.
Oh, G. et al., "Bulk-Type All Solid-State Batteries with 5 V Class LiNi0.5Mn1.5O4 Cathode and Li10GeP2S12 Solid Electrolyte", Chem. Mater., 2016, 28, pp. 2634-2640.
Ohtomo, Takamasa, et al., "Characteristics of the Li2O—Li2S—P2S5 glasses synthesized by the two-step mechanical milling, Journal of Non-Crystalline Solids," 2013, vol. 364, pp. 57-61.
Ohtomo, Takamasa, et al., "Electrical and electrochemical properties of Li2S—P2O5 glass-ceramic electrolytes", Journal of Power Sources, 2005, vol. 146, pp. 715-718.
Ohtomo, Takamasa, et al., "Suppression of H2S gas from Li2S—P2S5 glass electrolytes by the addition of Li2O", The Electrochemical Society, Abstract #1189, Honolulu PRIME 2012, 1 page.
Ong, S. et al., "Phase stability, electrochemical stability and ionic conductivity of the Li10±1MP2X12 (M=Ge, Si, Sn, Al or P and X=O, S or Se) family of superionic conductors," Energy Environ. Sci., 2013, 6, pp. 148-156.
Ooura, Yuji et al., "A new lithium-ion conducting glass ceramic in the composition of 75Li2S·5P2S3·20P2S5(mol%)", Solid State Ionics 2014, vol. 262, pp. 733-737.
Patil, Deepak S. et al., "Ionic conductivity study of Lil-Ga2S3—GeS2 chalcogenide glasses using a random-walk Approach", Pure Appl. Chem., 2014, pp. 1-11; DOI: 10.1515/pac-2014-1005.
Peutzfeldt, Anne et al., "Resin composites in dentistry: the monomer systems", Eur J Oral Sci, 1997, vol. 105, pp. 97-116.
Pham, Ha Q. et al., "Epoxy Resins", Ullmann's Encylclopedia of Industrial Chemistry, vol. 13, 2012, Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim, pp. 155-244.
Pradel, A., et al., "Ionically Conductive Chalcogenide Glasses", Journal of Solid State Chemistry, 1992, vol. 96, pp. 247-257.
Pradel, A., et al., "Lithium Chalcogenide Conductive Glasses", Materials Chemistry and Physics, 1989, vol. 23, pp. 121-142.
Qu, Meng et al., "Nanomechanical Quantification of Elastic, Plastic, and Fracture Properties of LiCoO2", Adv. Energy Mater., 2012, vol. 2, pp. 940-944.
Rangasamy et al., "An Iodide-Based Li7P2S8I Superionic Conductor," J. Am. Chem. Soc., 2015, vol. 137, pp. 1384-1387.
Rangasamy et al., "Heteroclite electrochemical stability of an I based Li7P2S8I superionic conductor", Angewandte Chemie: https://www.osti.gov/pages/servlets/purl/1185568.
Rao, R. Prasada, et al., "Synthesis and Li+ ion Migration Studies of Li6PS5X (X=C1, Br, I)", Mater. Res. Soc. Symp. Proc., 2011, vol. 1331, DOI: 10.1557/opl.2011.41 24; 6 pages.
Rao, Rayavarapu et al., "Variation in structure and Li30 -ion migration in argyrodite-type Li6PS5X (X=Cl, Br, I) solid electrolytes", J. Solid State Electrochem, 2012, vol. 16, pp. 1807-1813.
Response to the Communication dated Jul. 12, 2019 filed on Jan. 20, 2020 for Application No. EP16871533.2; 4 pages.
Sahu, Gayatri, et al., "Air-Stable, High-Conduction Solid Electrolytes of Arsenic-Substituted Li4SnS4", Energy & Environmental Science, 2014, vol. 7, pp. 1053-1058.
Sakuda, Atsushi et al., "Evaluation of elastic modulus of Li2S—P2S5 glassy solid electrolyte by ultrasonic sound velocity measurement and compression test", 2013, Journal of the Ceramic Society of Japan 121 [11], pp. 946-949, 4 pages.
Sakuda, Atsushi, et al., "All-solid-state lithium secondary batteries using LiCoO2 particles with pulsed laser deposition coatings of Li2S—P2S5 solid electrolytes", Journal of Power Sources, 2011, vol. 196, pp. 6735-6741.
Sakuda, Atsushi, et al., "Sulfide Solid Electrolyte with Favorable Mechanical Property for All-Solid-State Lithium Battery," Scientific Reports, 2013, 3:2261, DOI: 10.1038/srep02261, 5 pages.
Second Office Action of Japanese Patent Application No. 2018-528692 dated Sep. 7, 2021, along with the English translation.
Seino, Yoshikatsu, et al., "A sulphide lithium super ion conductor is superior to liquid ion conductors for use in rechargeable batteries", Energy & Environmental Science, 2014, vol. 7, pp. 627-631.
Seino, Yoshikatsu, et al., "Synthesis and electrochemical properties of Li2S—B253—LLISiO4", Solid State Ionics, 2006, vol. 177, pp. 2601-2603.
Seino, Yoshikatsu, et al., "Synthesis of phosphorous sulfide solid electrolyte and all-solid-state lithium batteries with graphite electrode", Solid State Ionics, 2005, pp. 2389-2393.
Seino, Yoshikatsu, et al., Electronic Supplementary Material (ESI) for Energy & Environmental Science, This journal is © The Royal Society of Chemistry, 2014, 4 pages.
Seo, Inseok, et al., "Fast lithium ion conducting solid state thin-film electrolytes based on lithium thio-germanate materials", Acta Materialia, 2011, vol. 59, pp. 1839-1846.
Seo, Inseok, et al., "Structural Properties of Lithium Thio-Germanate Thin Film Electrolytes Grown by Radio Frequency Sputtering," Inorganic Chemistry, 2011, vol. 50, pp. 2143-2150.
Shafizadeh, F. et al. "Thermal degradation of cellulose in air and nitrogen at low temperatures," Journal of Applied Polymern Science, vol. 23, Issue 5, Mar. 1, 1979, pp. 1431-1442.
Sistla, Ramesh, K. et al., "Structural studies on xLi2S-(1-x)P2S5 glasses by X-ray diffraction and molecular dynamics simulation", Journal of Non-Crystalline Solids, 2004, vol. 349, pp. 54-59.
Skaarup, Steen et al., "Mixed Phase Solid Electrolytes With Nonconducting Polymer Binder", Solid State Ionics, 1990, 40/41, pp. 1021-1024.
Skaarup, Steen et al., "Mixed Phase Solid Electrolytes", Solid State Ionics, 1988, vol. 28-30, pp. 975-978.
Skelhorn, David, "Particulate Fillers in Elastomers", Particulate-filled polymer composites, 2nd Edition, Shawbury: Rapra Technology Limited, 2003, pp. 303-356.
Sun, Y. et al., "Oxygen substitution effects in Li10GeP2S12 solid electrolyte", Journal of Power Sources, 2016, vol. 324, pp. 798-803.
Suzuki, K. et al., "Synthesis, structure, and electrochemical properties of crystalline Li—P—S—O solid electrolytes: Novel lithium-conducting oxysulfides of Li10GeP2S12 family", Solid State Ionics, vol. 288, May 2016, pp. 229-234.
Sveinbjornsson, Dadi, et al., "Ionic Conductivity and the Formation of Cubic CaH2 in the LiBH4—Ca(BH4)2 Composit", Journal of Solid State Chemistry, 2014, vol. 211, pp. 81-89.
Tachez, Michel, et al., "Ionic Conductivity of and Phase Transition in Lithium Thiophosphate Li3PS4", Solid State Ionics, 1984, vol. 14, pp. 181-185.
Takada et al., "Solid-state lithium battery with graphite anode", Solid State Ionics, Mar. 1, 2003, vol. 158, No. 3-4, pp. 269-274.
Takada, K. et al., "Compatibility of Lithium Ion Conductive Sulfide Glass with Carbon-Lithium Electrode", J. Electrochem. Soc. 2003, vol. 150, No. 3, pp. A274-A277.
Takada, Kazunori, et al., "Electrochemical behaviors of Li+ ion conductor Li3PO4—Li2S—SiS2", Journal of Power Sources, 1993, vol. 43-44, pp. 135-141.
Takada, Kazunori, et al., "Lithium ion conductive oxysulfide Li3PO4—Li3PS4", Solid State Ionics, 2005, vol. 176, pp. 2355-2359.
Takada, Kazunori, et al., "Solid State Lithium Battery with Oxysulfide glass", Solid State Ionics, 1996, vol. 86-88, pp. 877-882.
Takahara, Hikari, et al., "Application of Lithium Metal Electrodes to All-Solid-State Lithium Secondary Batteries Using Li3PO4−Li2S—SiS2 glass", Journal of the Electrochemical Society, 2004, vol. 151, No. 9, pp. A1309-A1313.
Tarhouchi, I. et al., "Electrochemical characterization of Li10SnP2S12 : An electrolyte or a negative electrode for solid state Li-ion batteries?", Solid State Ionics, vol. 296, 2016, pp. 18-25.
Tatsumisago, Masahiro, et al., "All-solid-state lithium secondary batteries using sulfide-based glass-ceramic electrolytes", Journal of Power Sources, 2006, vol. 159, pp. 193-199.
Teragawa, Shingo, et al., "Preparation of Li2S—P2S5 solid electrolyte from N-methylformamide solution and application for all-solid-state lithium battery", Journal of Power Sources, 2014, vol. 248, pp. 939-942.
Thokchom, Joykumar S. et al., "Ionically Conducting Composite Membranes from the Li2O—Al2O3—TiO2—P2O5 Glass-Ceramic", J. Am. Ceram. Soc., 90 [2], 2007, pp. 462-466.
Trevey, James, et al., "Glass-ceramic Li2S—P2S5 electrolytes prepared by a single step ball billing process and their application for all-solid-state lithium-ion batteries", Electrochemistry Communications, 2009, vol. 11, pp. 1830-1833.
Ujiie, Satoshi et al., "Conductivity of 70Li2S·30P2S5 glasses and glass-ceramics added with lithium halides", Solid State Ionics, vol. 263, 2014, pp. 57-61.
Ujiie, Satoshi, et al., "Preparation and electrochemical characterization of (100-x)(0.7Li2S·0.3P2S5) xLiBr glass-ceramic electrolytes", Mater Renew Sustain Energy, 2014, 3:18, pp. 1 of 8; DOI 10.1007/s40243-013-0018-x.
Villaluenga et al., "Compliant glass-polymer hybrid single ion-conducting electrolytes for lithium batteries", PNAS, Jan. 5, 2016, vol. 113, No. 1, pp. 52-57.
Wada, H. et al., "Preparation and Ionic Conductivity of New B2S3—Li2S—Lil Glasses", Mat. Res. Bull., 1983, vol. 18, pp. 189-193.
Wall, L.A. et al., "The Depolymerization of Polymethylene and Polyethylene", J. Am. Chem. Soc., 1954, vol. 76 (13), pp. 3430-3437.
Wang, Y. et al., "Highly lithium-ion conductive thio-LISICON thin film processed by low-temperature solution method", Journal of Power Sources, 2013, vol. 224, pp. 225-229.
Wang, Y. et al., "Highly lithium-ion conductive thio-LISICON thin film processed by low-temperature solution method", Supporting Information, Journal of Power Sources, 2013, vol. 224, pp. 225-229.
Wang, Yan-Jie et al., "Characterization of [Poly(ethylene oxide)] LiClO—Li1.3Al0.3Ti1.7(PO4)3 Composite Polymer Electrolytes with Poly(ethylene oxide)s of Different Molecular Weights", Journal of Applied Polymer Science, 2006, vol. 102, pp. 1328-1334.
Wang, Yiqun et al., "X-ray photoelectron spectroscopy for sulfide glass electrolytes in the systems Li2S—P2S5 and Li2S—P2S5—LiBr", Journal of the Ceramic Society of Japan, 2016, vol. 124, No. 5, pp. 597-601.
Weber, Dominik A. et al., "Structural Insights and 3D Diffusion Pathways within the Lithium Superionic Conductor Li10GeP2S12", Chem. Mater., 2016, 28, pp. 5905-5915.
Wenzel, S. et al., "Direct Observation of the Interfacial Instability of the Fast Ionic Conductor Li10GeP2S12at the Lithium Metal Anode", Chem. Mater., 2016, vol. 28, pp. 2400-2407.
Westerhout, R. W. J. et al., "Kinetics of the Low-Temperature Pyrolysis of Polyethene, Polypropene, and Polystyrene Modeling, Experimental Determination, and Comparison with Literature Models and Data," Ind. Eng. Chem. Res., 1997, 36 (6), pp. 1955-1964.
Wieczorek et al., "Composite Polymeric Electrolytes", Electronic Materials: Science and Technology, 2008, vol. 10, pp. 1-70.
Wright, Charles D., "Epoxy Structural Adhesives," Structural Adhesives: Chemistry and Technology, Springer Science & Business Media, Dec. 6, 2012, pp. 113-179.
Xu et al., "One-dimensional stringlike cooperative migration of lithium ions in an ultrafast ionic conductor", Appl. Phys. Lett., vol. 101, 2012, 031901.
Yamashita et al., "Formation and ionic conductivity of Li2S—GeS2—Ga2S3 glasses and thin films", Solid State Ionics, 2003, vol. 158, pp. 151-156.
Yamauchi et al., "Preparation and ionic conductivities of (100-x)(0.75Li2S·0.25P2S5)·xLiBH4 glass electrolytes", Journal of Power Sources, 2013, vol. 244, pp. 707-710.
Yubuchi et al., "Preparation of high lithium-ion conducting Li6PS5Cl solid electrolyte from ethanol solution for all-solid-state lithium batteries", Journal of Power Sources, 2015, vol. 293, pp. 941-945.
Zhang, Hanjun (Henry) et al., "Preparation and characterization of composite electrolytes based on PEO(375)-grafted fumed silica", Solid State Ionics, vol. 178, 2008, pp. 1975-1983.
Zhu, Zhuoying et al., "Li3Y(PS4)2 and Li5PS4Cl2: New Lithium Superionic Conductors Predicted from Silver Thiophosphates using Efficiently Tiered Ab Initio Molecular Dynamics Simulations," Chem. Mater., 2017, vol. 29 (6), pp. 2474-2484.
Zhu, Zhuoying et al., "Li3Y(PS4)2 and Li5PS4Cl2: New Lithium Superionic Conductors Predicted from Silver Thiophosphates using Efficiently Tiered Ab Initio Molecular Dynamics Simulations," Chem. Mater., 2017, vol. 29, No. 6, pp. 2474-2484, and Supporting Information, 13 pages.

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US12074276B2 (en) 2018-11-06 2024-08-27 Quantumscape Battery, Inc. Electrochemical cells with catholyte additives and lithium-stuffed garnet separators
US11967676B2 (en) 2021-11-30 2024-04-23 Quantumscape Battery, Inc. Catholytes for a solid-state battery
US11962002B2 (en) 2021-12-17 2024-04-16 Quantumscape Battery, Inc. Cathode materials having oxide surface species

Also Published As

Publication number Publication date
EP3504749A1 (en) 2019-07-03
US20190198838A1 (en) 2019-06-27
US20220328933A1 (en) 2022-10-13
EP3504749A4 (en) 2020-05-06
WO2018044952A1 (en) 2018-03-08
US12057600B2 (en) 2024-08-06

Similar Documents

Publication Publication Date Title
US12057600B2 (en) Catholytes for solid state rechargeable batteries, battery architectures suitable for use with these catholytes, and methods of making and using the same
US11881596B2 (en) Solid electrolyte separator bonding agent
EP3469648B1 (en) High energy density, high power density, high capacity, and room temperature capable &#34;anode-free&#34; rechargeable batteries
JP6999425B2 (en) Lithium ion gel battery
US10553903B2 (en) Electrolyte for lithium secondary battery and lithium secondary battery including the same
US7592102B1 (en) Electrolyte for lithium ion secondary battery and lithium ion secondary battery comprising the same
KR101607024B1 (en) Lithium secondary battery
US20210273291A1 (en) Catholyte management for a solid-state separator
WO2003083974A1 (en) Method for fabricating composite electrodes
US10283810B2 (en) Lithium-ion battery
US12074276B2 (en) Electrochemical cells with catholyte additives and lithium-stuffed garnet separators
US11967676B2 (en) Catholytes for a solid-state battery
KR101588616B1 (en) Lithium secondary battery having Improved Low-temperature discharge property and Room-temperature lifespan characteristics
KR20180117868A (en) Electrolyte for lithium secondary battery and lithium secondary battery comprising thereof
KR20200126781A (en) Non-aqueous electrolyte for lithium secondary battery and lithium secondary battery comprising the same
US20220131191A1 (en) Electrolyte solution for lithium secondary battery and lithium secondary battery including the same
CN103608963A (en) Liquid electrolyte for lithium accumulator, containing a ternary mixture of non-aqueous organic solvents

Legal Events

Date Code Title Description
FEPP Fee payment procedure

Free format text: ENTITY STATUS SET TO UNDISCOUNTED (ORIGINAL EVENT CODE: BIG.); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY

AS Assignment

Owner name: QUANTUMSCAPE CORPORATION, CALIFORNIA

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:ROBERTS, GREG;CHEN, ZHEBO;HUDSON, WILL;AND OTHERS;SIGNING DATES FROM 20190405 TO 20190530;REEL/FRAME:049366/0932

STPP Information on status: patent application and granting procedure in general

Free format text: DOCKETED NEW CASE - READY FOR EXAMINATION

STPP Information on status: patent application and granting procedure in general

Free format text: NON FINAL ACTION MAILED

AS Assignment

Owner name: QUANTUMSCAPE SUBSIDIARY, INC., CALIFORNIA

Free format text: CHANGE OF NAME;ASSIGNOR:QUANTUMSCAPE CORPORATION;REEL/FRAME:055614/0869

Effective date: 20201125

AS Assignment

Owner name: QUANTUMSCAPE BATTERY, INC., CALIFORNIA

Free format text: CHANGE OF NAME;ASSIGNOR:QUANTUMSCAPE SUBSIDIARY, INC.;REEL/FRAME:055665/0765

Effective date: 20210119

STPP Information on status: patent application and granting procedure in general

Free format text: RESPONSE TO NON-FINAL OFFICE ACTION ENTERED AND FORWARDED TO EXAMINER

STPP Information on status: patent application and granting procedure in general

Free format text: NON FINAL ACTION MAILED

STPP Information on status: patent application and granting procedure in general

Free format text: RESPONSE TO NON-FINAL OFFICE ACTION ENTERED AND FORWARDED TO EXAMINER

STPP Information on status: patent application and granting procedure in general

Free format text: NOTICE OF ALLOWANCE MAILED -- APPLICATION RECEIVED IN OFFICE OF PUBLICATIONS

STPP Information on status: patent application and granting procedure in general

Free format text: PUBLICATIONS -- ISSUE FEE PAYMENT RECEIVED

STPP Information on status: patent application and granting procedure in general

Free format text: PUBLICATIONS -- ISSUE FEE PAYMENT VERIFIED

STCF Information on status: patent grant

Free format text: PATENTED CASE

MAFP Maintenance fee payment

Free format text: PAYMENT OF MAINTENANCE FEE, 4TH YEAR, LARGE ENTITY (ORIGINAL EVENT CODE: M1551); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY

Year of fee payment: 4